Thermodynamic Properties of Organic Compounds and Their Mixtures

Landolt-Börnstein Numerical Data and Functional Relationships in Science and Technology New Series / Editor in Chief: W...

57 downloads 1215 Views 2MB Size Report

This content was uploaded by our users and we assume good faith they have the permission to share this book. If you own the copyright to this book and it is wrongfully on our website, we offer a simple DMCA procedure to remove your content from our site. Start by pressing the button below!

Report copyright / DMCA form

DOWNLOAD PDF

Landolt-Börnstein Numerical Data and Functional Relationships in Science and Technology New Series / Editor in Chief: W. Martienssen

Group IV: Physical Chemistry Volume 8

Thermodynamic Properties of Organic Compounds and their Mixtures Subvolume G Densities of Alcohols

M. Frenkel, X. Hong, R.C. Wilhoit, K.R. Hall

Edited by K.R. Hall and K.N. Marsh

12 3

ISSN 0942-7996 (Physical Chemistry) ISBN 3-540-66233-2 Springer-Verlag Berlin Heidelberg New York Library of Congress Cataloging in Publication Data Zahlenwerte und Funktionen aus Naturwissenschaften und Technik, Neue Serie Editor in Chief: W. Martienssen Vol. IV/8G: Editors: K.R. Hall, K.N. Marsh At head of title: Landolt-Börnstein. Added t.p.: Numerical data and functional relationships in science and technology. Tables chiefly in English. Intended to supersede the Physikalisch-chemische Tabellen by H. Landolt and R. Börnstein of which the 6th ed. began publication in 1950 under title: Zahlenwerte und Funktionen aus Physik, Chemie, Astronomie, Geophysik und Technik. Vols. published after v. 1 of group I have imprint: Berlin, New York, Springer-Verlag Includes bibliographies. 1. Physics--Tables. 2. Chemistry--Tables. 3. Engineering--Tables. I. Börnstein, R. (Richard), 1852-1913. II. Landolt, H. (Hans), 1831-1910. III. Physikalisch-chemische Tabellen. IV. Title: Numerical data and functional relationships in science and technology. QC61.23 502'.12 62-53136 This work is subject to copyright. All rights are reserved, whether the whole or part of the material is concerned, specifically the rights of translation, reprinting, reuse of illustrations, recitation, broadcasting, reproduction on microfilm or in other ways, and storage in data banks. Duplication of this publication or parts thereof is permitted only under the provisions of the German Copyright Law of September 9, 1965, in its current version, and permission for use must always be obtained from SpringerVerlag. Violations are liable for prosecution act under German Copyright Law. © Springer-Verlag Berlin Heidelberg 1998 Printed in Germany The use of general descriptive names, registered names, trademarks, etc. in this publication does not imply, even in the absence of a specific statement, that such names are exempt from the relevant protective laws and regulations and therefore free for general use. Product Liability: The data and other information in this handbook have been carefully extracted and evaluated by experts from the original literature. Furthermore, they have been checked for correctness by authors and the editorial staff before printing. Nevertheless, the publisher can give no guarantee for the correctness of the data and information provided. In any individual case of application, the respective user must check the correctness by consulting other relevant sources of information. Cover layout: Erich Kirchner, Heidelberg Typesetting: Authors and Redaktion Landolt-Börnstein, Darmstadt Printing: Computer to plate, Mercedes-Druck, Berlin Binding: Lüderitz & Bauer, Berlin SPIN: 10735217

63/3020 - 5 4 3 2 1 0 – Printed on acid-free paper

Editors K.R. Hall Thermodynamics Research Center TheTexas A&M University System College Station, Texas 77843-3111, USA

K.N. Marsh former Thermodynamics Research Center TheTexas A&M University System College Station, Texas 77843-3111, USA now Department of Chemical and Process Engineering University of Canterbury Christchurch, New Zealand

Authors M. Frenkel X. Hong R.C. Wilhoit K.R. Hall Thermodynamics Research Center TheTexas A&M University System College Station, Texas 77843-3111, USA

Landolt-Börnstein Editorial Office Gagernstr. 8, D-64283 Darmstadt, Germany fax: +49 (6151) 171760 e-mail: [email protected] Internet http://science.springer.de/newmedia/laboe/lbhome.htm Helpdesk e-mail: [email protected]

Preface

Critically evaluated experimental data covering the densities of organic compounds is essential for both scientific and industrial applications. Knowledge of densities is important in many areas, including custody transfer of materials, product specification, development of various predictive methods, and for characterizing compounds and estimating their purity. Various compilations of densities for organic compounds have been published. The early LandoltBörnstein compilation [23-ano] contained recommended values at specific temperatures. International Critical Tables [28-ano-1] provided recommended densities at 0 °C and values of constants for either a second or third order polynomial equation to represent densities as a function of temperature. This compilation also gave the range of validity of the equation and the limits of uncertainty, references used in the evaluation and those not considered. This compilation is one of the most comprehensive ever published. Timmermans [50-tim, 65-tim], Dreisbach [55-dre, 59-dre, 61-dre] and Landolt-Börnstein [71-ano] published additional compilations, primarily of experimental data. These compilations contained experimental data along with reference sources but no estimates of uncertainty for the data nor recommended values. The Thermodynamics Research Center has published recommended values for the densities of organic compounds since 1942 in its two loose leaf publications: TRC Thermodynamic Tables Hydrocarbons and Non-Hydrocarbons. These compilations are updated with four supplements per year. References to the literature values used in the selection and those not used in the selection appear in the references for each table. The accuracy of the values is apparent from the number of significant figures provided. More recently, the Design Institute of Physical Property Data, Project 801 has assembled a set of recommended equations for the densities of over 1500 compounds [89-dau/dan, 91-dau/dan, 92-dau/dan, 93-dau/dan, 94-dau/dan, 95-dau/dan, 96-daudan, 97-daudan]. Densities are represented by an equation fit to selected values from the freezing temperature to the critical temperature. References to sources of data used in the evaluation and those not used are given along with a quality assessment. In many cases, the equation does not fit density values at intermediate temperatures, especially at 293.15 K and 298.15 K, within the experimental uncertainty. Thus, the equation is not useful for purity comparisons, custody transfer, or product specification when the highest accuracy is required. Smith and Srivastava [86-smi/sri, 86-smi/sri-1] recently have published a compilation (in two volumes) which contains recommended values in tabular form as well as equations with statistical information regarding the fit. However, this compilation contains no indication of data quality or uncertainties. The present volume contains densities for non-cyclic alcohols including monoalcohols, diols, and triols both fully saturated and with various extents of unsaturation which have been collected from the literature published from 1870 to early 1999. The various compilations listed above also have been consulted for sources of original data. This volume continues our effort in evaluation of the densities of organic compounds [see volume IV/8B [96-wil/mar] for the densities of alkanes, volume IV/8C [96-wil/mar-1] for the densities of alkenes, alkynes and alkadienes, volume IV/8D [97-wil/hon] for the densities of monocyclic non-aromatic hydrocarbons, volume IV/8E [98-wil/hon] for the densities of aromatic hydrocarbons, volume IV/8F [99-wil/hon] for the densities of polycyclic hydrocarbons]. All experimental density values have been evaluated critically and assigned numerical uncertainties individually. These assessments have been used to derive an equation to fit the data and to obtain recommended values with uncertainties. Detailed evaluation procedures appear in Chapter 1. Algorithms for the automatic selection of data used in the fit and for the selection of the type of equation and order of polynomial have been developed. The algorithms depend upon the assigned uncertainties, the distribution of density values over the experimental temperature range, and the magnitude and distribution of differences between observed and smoothed values. These algorithms can fit any kind of data to a function of independent variables. We have collected data for 829 compounds, consisting of data sets drawn from 1119 sources.

The volume contains six chapters; a list of references, and two indexes (Chemical Abstracts Service Registry Number Index and Chemical Name Index). Chapter 1 contains: a short introduction; a description of the tables; a detailed description of the methods used in the evaluation, selection and smoothing process; a glossary of symbols and a description of the order of compounds in the Tables used. Chapter 2 covers the monoalcohols, Chapter 3 contains the data for diols, and Chapter 4 has the triols. The tables contain the original literature data along with their estimated uncertainties and the evaluated data in both numerical form and as coefficients to equations with selected statistical information. When data cover a sufficient temperature range, graphical plots of the deviations of the experimental data from the recommended equation are given. The chemical name index contains the IUPAC names for the compounds, as well as alternate names that often appear in practice. This volume should be useful to a wide community of researchers, data specialists, and engineers working in the field of physical and organic chemistry, chemical engineering, material science, environmental chemistry, chemical aspects of energy technology, and those engaged in the development of new predictive procedures. The book should also be of use to students and faculty in Chemistry and Chemical Engineering departments at universities as a reference book of evaluated thermophysical properties.

Acknowledgments The authors wish to express their sincere appreciation to staff members of the Thermodynamics Research Center (TRC), part of the Chemical Engineering Division of the Texas Engineering Experiment Station in The Texas A&M University System. Our special thanks to Munaf Chasmawala and Cheryl Clark for their assistance in data collection and entry, formatting the text, preparing the graphs, and composing the camera-ready copy of the manuscript.

College Station, June 1999

M. Frenkel, X. Hong, R.C. Wilhoit, K.R. Hall

References 23-ano

Landolt-Börnstein Physikalisch-Chemische Tabellen, 5. Auflage, Hauptwerk, Band 1. Roth, W.A., Scheel, K. (eds.), Berlin: Springer-Verlag, 1923.

28-ano-1

International Critical Tables of Numerical Data, Physics, Chemistry and Technology Vol. III. Washburn, E.W. (ed.), New York: McGraw-Hill, 1928.

50-tim

Timmermans, J.: Physico-Chemical Constants of Pure Organic Compounds, Vol. 1. New York: Elsevier, 1950.

55-dre

Dreisbach, R.R.: Physical Properties of Chemical Compounds, Advances in Chemistry Series No. 15. Washington, D.C.: Am. Chem. Soc., 1955.

59-dre

Dreisbach, R.R.: Physical Properties of Chemical Compounds - II, Advances in Chemistry Series No. 22. Washington, D.C: Am. Chem. Soc., 1959.

61-dre

Dreisbach, R.R.: Physical Properties of Chemical Compounds, Advances in Chemistry Series No. 29. Washington, D.C.: Am. Chem. Soc., 1961.

65-tim

Timmermans, J.: Physico-Chemical Constants of Pure Organic Compounds, Vol. II. New York: Elsevier, 1965.

71-ano

Landolt-Börnstein Sechste Auflage, II. Band, Eigenschaften der Materie in ihren Aggregatzuständen, 1. Teil, Mechanisch-thermische Zustandsgrössen. Berlin: Springer-Verlag, 1971.

86-smi/sri

Smith, B.D., Srivastava, R.: Thermodynamic Data for Pure Compounds, Part B. Halogenated Hydrocarbons and Alcohols. New York: Elsevier, 1986.

86-smi/sri-1

Smith, B D., Srivastava, R.: Thermodynamic Data for Pure Compounds, Part A. Hydrocarbons and Ketones. New York: Elsevier, 1986.

89-dau/dan

Daubert, T.E., Danner, R.P.: Physical and Thermodynamic Properties of Pure Chemicals: Data Compilation. London: Taylor & Francis, 1989.

91-dau/dan

Daubert, T.E., Danner, R.P.: Physical and Thermodynamic Properties of Pure Chemicals: Data Compilation, Supplement 1. London: Taylor & Francis, 1991.

92-dau/dan

Daubert, T.E., Danner, R.P.: Physical and Thermodynamic Properties of Pure Chemicals: Data Compilation, Supplement 2. London: Taylor & Francis, 1992.

93-dau/dan

Daubert, T.E., Danner, R.P.: Physical and Thermodynamic Properties of Pure Chemicals: Data Compilation, Supplement 3. London: Taylor & Francis, 1993.

94-dau/dan

Daubert, T.E., Danner, R.P.: Physical and Thermodynamic Properties of Pure Chemicals: Data Compilation, Supplement 4. London: Taylor & Francis, 1994.

95-dau/dan

Daubert, T.E., Danner, R.P.: Physical and Thermodynamic Properties of Pure Chemicals: Data Compilation, Supplement 5. London: Taylor & Francis, 1995.

96-dau/dan

Daubert, T.E., Danner, R.P.: Physical and Thermodynamic Properties of Pure Chemicals: Data Compilation, Supplement 6. London: Taylor & Francis, 1996.

96-wil/mar

Wilhoit, R.C., Marsh, K.N., Hong, X., Gadalla, N., Frenkel, M.: Densities of Aliphatic Hydrocarbons: Alkanes. Landolt-Börnstein, New Series, Vol. IV/8B, Berlin: Springer-Verlag, 1996.

96-wil/mar-1

Wilhoit, R.C., Marsh, K.N., Hong, X., Gadalla, N., Frenkel, M.: Densities of Aliphatic Hydrocarbons: Alkenes, Alkadienes, Alkynes and Miscellaneous Compounds. Landolt-Börnstein, New Series, Vol. IV/8C, Berlin: Springer-Verlag, 1996.

97-dau/dan

Daubert, T.E., Danner, R.P.: Physical and Thermodynamic Properties of Pure Chemicals: Data Compilation, Supplement 7. London: Taylor & Francis, 1997.

97-wil/hon

Wilhoit, R.C., Hong, X., Frenkel, M., Hall, K.R.: Densities of Monocyclic Hydrocarbons. Landolt-Börnstein, New Series, Vol. IV/8D, Berlin: Springer-Verlag, 1997.

98-wil/hon

Wilhoit, R.C., Hong, X., Frenkel, M., Hall, K.R.: Densities of Aromatic Hydrocarbons. Landolt-Börnstein, New Series, Vol. IV/8E, Berlin: Springer-Verlag, 1998.

99-wil/hon

Wilhoit, R.C., Hong, X., Frenkel, M., Hall, K.R.: Densities of Polycyclic Hydrocarbons. Landolt-Börnstein, New Series, Vol. IV/8F, Berlin: Springer-Verlag, 1999.

1.1 Basic Concepts

1

1 Introduction

1.1 Basic Concepts The mass density of a substance is an intensive quantity defined by:

ρ = m/v

(1.1)

where m is the mass and v is the volume of the sample. Both these quantities are extensive quantities. Other densities often referred to in the literature are the relative density and the molar density. Relative density, also called specific gravity, is:

ρr = ρ / ρ0

(1.2)

where ρ0 is the density of a standard substance. It is necessary to specify the conditions of temperature and pressure for the standard substance. The most common reference material is water often at the temperature of its maximum density, 4 °C, at atmospheric pressure. The molar density is defined as

ρm = 1/V

(1.3)

where V is the volume occupied by one mole of the substance. The only densities reported in this volume are the mass densities; relative and molar densities have been converted to mass densities, and all densities have been reported in SI units. If the mass, m, in equation (1.1) has not been corrected for air bouancy it gives the apparent density in air. The API specific gravity is: ρ (API) = 141.5/ρr – 131.5, in which ρr is ρ(288.68 K)/ρο(288.68 K), and the standard substance is water at 288.68 K (60 °F). The density of a material is a function of temperature and pressure but its value at some standard condition (for example, 293.15 K or 298.15 K at either atmospheric pressure or at the vapor pressure of the compound) often is used to characterize a compound and to ascertain its purity. Accurate density measurements as a function of temperature are important for custody transfer of materials when the volume of the material transferred at a specific temperature is known but contracts specify the mass of material transferred. Engineering applications utilize the density of a substance widely, frequently for the efficient design and safe operation of chemical plants and equipment. The density and the vapor pressure are the most often-quoted properties of a substance, and the properties most often required for prediction of other properties of the substance. In this volume, we do not report the density of gases, but rather the densities of solids as a function of temperature at atmospheric pressure and the densities of liquids either at atmospheric pressure or along the saturation line up to the critical temperature. The purpose of this compilation is to tabulate the densities of compounds, hence only minimal description of experimental methods used to measure the density of liquids or solids appears. Detailed descriptions of methods for density determination of solids, liquids and gases, along with appropriate density reference standards, appear in a chapter by Davis and Koch in Physical Methods of Chemistry, Volume VI, Determination of Thermodynamic Properties [86-ros/bae]. The two principal experimental apparatuses used to determine the density of a liquid are: the pycnometer and the vibrating tube densimeter. The pycnometer method involves measuring the mass of a liquid in a vessel of known volume. The volume of the pycnometer, either at the temperature of measurement or at some reference temperature, is determined using a density standard, usually water or mercury. Using considerable care and a precision analytical balance accurate to ±10-5 g, it is possible to achieve densities accurate to a few parts in 106 with a pycnometer having a volume of 25 cm3 to 50 cm3.

Landolt-Börnstein New Series IV/8G

2

1.1 Basic Concepts - 1.2 Scope of the Compilation

It is common to achieve accuracies of 1 part in 105 in using equation (1.1) with pycnometers as small as 5 cm3 and routine measurements can achieve 1 part in 104. However the main sources of error in assigning density to a particular compound in a particular state arise from factors other than the measurment of mass and volume. See Section 1.4.1 The vibrating tube densimeter relies upon the fact that the frequency f of vibration for a U or V shaped tube depends upon the mass of material in the tube:

ρ = A/ f 2 + B

(1.4)

Calibration of the apparatus is necessary; usually water and air or nitrogen are the reference materials. Vibrating tube densimeters designed to operate close to atmospheric pressure can achieve repeatability of parts in 106. If the reciprocal of the frequency is linear in density, accuracies of 1 part in 105 are readily achievable. The principal experimental method used to measure the density of a solid is determination of the mass of liquid displaced by a known mass of solid. It is essential that the solid have no appreciable solubility in the liquid, that all occluded air be removed from the solid and that the density of the displacement fluid be less than that of the solid lest the solid float. Densities of crystalline solids also can be determined from the dimensions of the unit cell. Davis and Koch discuss other methods for measuring the density of liquids and solids such as: hydrostatic weighing of a buoy and flotation methods.

1.2 Scope of the Compilation Volume IV/8G presents observed values for the densities of non-cyclic alcohols. These values represent a compilation and evaluation of data from the scientific literature covering approximately the past 100 years. The values presented come from the TRC Source Database. The Thermodynamics Research Center has assembled these data over a period of years and has used them to provide the evaluated density values listed in the TRC Thermodynamic Tables - Non-Hydrocarbons. An additional literature search has been performed immediately before producing this compilation to locate new or missing data and to bring the collection up-to-date. This compilation should include at least 90% of the pertinent data reported in the literature. The usual experimental conditions are in contact with air at one atmosphere below the normal boiling point, and in equilibrium with the vapor phase above the normal boiling point. In the summary tables, temperatures reported on the Kelvin scale have been obtained by adding 273.15 to temperatures originally given on the Celsius scale. Densities have units of kilograms per cubic meter (kg⋅m-3). Values reported in units of grams per milliliter, where the liter is “the volume of one kilogram of water at its temperature of maximum density” convert to kg⋅m-3 when multiplied by 999.972 (as defined by the 12th General Conference of the International Committee on Weights and Measure, 1964). Values of specific gravity relative to water at a stated reference temperature become density upon multiplication by the accepted density of water at the reference temperature. Most reported densities for liquids below the boiling point apply to the airsaturated liquid. Compounds are identified by an IUPAC approved name [93-ano-1], the empirical molecular formula, and the Chemical Abstracts Service Registry Number. A summary table is available for each compound which includes the reported temperature and density values, an assigned uncertainty for the density, the difference between the observed and smoothed density values and an index key to the source of the data. A complete list of references, identified by the index keys, appears at the end of the volume. Where appropriate, tables of smoothed, recommended values are given at integral multiples of 10 K over the experimental range of temperatures. Values at 293.15 K and 298.15 K are included when they are in the range of the original data set. The recommended values also have assigned uncertainties.

Landolt-Börnstein New Series IV/8G

1.3 Description of Tables - 1.4 Evaluation, Selection, and Smoothing of Data

3

1.3 Description of Data Tables Data for a particular compound are selected, evaluated and smoothed in one of four ways, depending upon the number and accuracy of the reported values and upon their distribution over the temperature range. Case 1. When the data set consists of at least four acceptable, effectively distinct values (see section 1.5.3), the densities in selected subsets are fit to a function of temperature using the least squares criterion. A summary table for the selected set gives the densities, their estimated uncertainties, the deviations between observed and calculated values, an index key to the list of references and a plotting symbol. If sufficient space remains, some data outside the selected set also are included in the summary table along with reference keys to any remaining data. A plot of the deviations between observed and calculated values is shown for the selected subset. Error bars indicate the size of the estimated uncertainties for the data. Distinct plotting symbols identify the five data sources that have the smallest average estimated uncertainties. A single symbol represents all remaining data in the selected set. A table consisting of smoothed, recommended values (calculated from the fitted functions) is also given. Estimated uncertainties are given for the recommended values which also appear as a continuous line on the deviation plot. Densities of crystal phases are in a separate section of the table. In most cases, these densities have not been fit as a function of temperature. Values of parameters, statistical measures of the fit, and references to sources of critical constants appear at the beginning of these sections. Case 2. For data sets that do not meet the criteria of Case 1, but contain acceptable values over a temperature range of at least two degrees, the results are smoothed using a linear function of temperature with an estimated coefficient of thermal expansion. A table of smoothed recommended values is presented. Case 3. For data sets that do not meet the criteria of either Case 1 or 2 but contain two or more values at a single temperature, a recommended value is given for this temperature by taking a weighted average of the observed values. Case 4. For data sets that contain only single values at one or two temperatures, the reported values are given rather than recommended values.

1.4 Evaluation, Selection and Smoothing of Data 1.4.1 Assignment of Uncertainties The Thermodynamics Research Center staff have assigned an uncertainty value to each observed and recommended density value listed in the tables. The true value of the property has a 95% probability of being in the range covered by + or – the uncertainty about the reported value. Assignment of uncertainty is a subjective evaluation based upon what is known about the measurement when the value is entered into the database, and includes the effects of all sources of experimental error. The errors have been propagated to the listed density at the reported temperature. Uncertainties reported by the investigators are considered but not necessarily adopted. Often, investigators report repeatability, but they usually do not provide uncertainty. Errors in density result from errors in temperature measurement or control; calibration of instruments; transfer, handling and weighing of samples; and impurities in the samples. At temperatures well below the critical temperature and near room temperature, standard techniques easily achieve accuracies of ±0.05%. For the compounds in this compilation, that level corresponds to about ±0.4 kg⋅m-3. Under these conditions, errors in temperature are not very significant. This level of accuracy only requires

Landolt-Börnstein New Series IV/8G

4

1.4 Evaluation, Selection, and Smoothing of Data

temperatures to be known within ± 0.5 K. At temperatures approaching the critical temperature, measurements become more demanding because of the rapid increase in the magnitude of the coefficient of thermal expansion. Greater accuracy, in general, requires careful attention to calibration, mass determination and sample handling techniques. It is assumed that values obtained by pycnometers have been corrected for buoyancy of air, unless the author specifically says otherwise. This correction increases the apparent density by 0.05 - 0.1%. When this correction has not been made, the estimated uncertainty is greater. Most measurements of densities of liquids below their normal boiling points are made in the presence of air. Densities reported here refer to liquids in equilibrium with a gas phase consisting of a mixture or air and vapor at a total pressure of one atmosphere below the normal boiling point and of vapor at the equilibrium vapor pressure above the boiling point. Thus air is not regarded as an impurity. A major source of error in most measurements is the presence of impurities in the sample. The effect of an impurity depends upon its amount in the sample and upon the difference between its density and the density of the principal constituent. Even when the sample purity is provided quantitatively, the impurities often are not identified individually. Nevertheless, a report of sample purity reduces the estimated uncertainty because it can be taken as evidence that the investigator has considered sample purity. The most ubiquitous impurity in liquids is water, and, because its density differs significantly from those of hydrocarbons, it is a common source of error. Exclusion of water requires that the sample be protected from the atmosphere during transfer, and that special precautions be taken to remove the sample from containers.

1.4.2 Quantitative Effect of Impurity on Density of Liquids The molar volume of a mixture of components, V, in terms of the mole fractions xi and partial molar volumes of the components Vi is: c

V = ∑ xiVi

(1.5)

i =1

For an ideal solution, the partial molal volumes equal the molar volumes of the pure liquid components. Denoting component the main components as 1 and the impurities as > 1, the volume becomes: c

V = x1V1 + ∑ x iVi

(1.6)

ρ = M /V

(1.7)

i =2

Then using,

and the molar mass of the mixture: c

M = ∑ xi M i

(1.8)

i =1

and assuming that the xi are small for i > 1, then

ρ=

c  ρ1   1 − ρ 1 ∑ wi vi   w1  i=2

(1.9)

where vi = Vi /Mi are partial specific volumes of the impurities and wi is the mass fraction of component i. Finally, the density of the mixture is related to the density of the main component and the impurities i by:

ρ=

c w ρ1  1 − ρ1 ∑ i  w1  i =2 ρi 

(1.10)

Landolt-Börnstein New Series IV/8G

1.4 Evaluation, Selection, and Smoothing of Data

5

The observed value of the density of a sample is sometimes presented as evidence of its purity. Assuming the sample contains a single impurity, equation (1.10) can be solved for ρ - ρ1:

ρ − ρ 1 = ρ 1 (1 − w1 − ρ 1 w2 / ρ 2 ) / w1

(1.11)

1.4.3 Procedure for Selection and Smoothing of Density Values - Case 1 A selected subset of the reported densities is fit to functions of temperature using the least squares criterion. Up to a boundary temperature Tb (approximately 0.8Tc), the calculated density ρx is represented by a polynomial in temperature with coefficients ak of order p, p

ρ x = ∑ ak T k .

(1.12)

k =0

Above Tb the smoothed values are given by a modification of the Guggenheim equation [67-gug]

)[

(

ρ x = 1 + 1.75θ + 0.75θ 3 ρ c + b1 (Tc − T ) + b2 (Tc − T ) + b3 (Tc − T ) + b4 (Tc − T ) 2

3

4

]

(1.13)

where Tc is the critical temperature and θ = (1-T/Tc)1/3. Selected values of critical constants are constant. Continuity with equation (1.12) results from forcing the two functions and their first derivatives with respect to temperature to be equal at the boundary. When no values are available above this temperature, only the polynomial is used. The following steps, implemented by a computer program written in C, generate the smoothed, recommended values. Input to the program consists of the set of observed density values, temperatures, estimated uncertainties, critical constants and values of certain parameters used by the program. Step 1. Separate the initial data into two sets, corresponding to temperatures above and below Tb. Step 2. Make an initial selection from the low temperature set by rejecting all points with zero uncertainty and all points with uncertainties above a limit determined by the data selection algorithm described in section 1.5.2. Zero uncertainties are assigned to values that are not experimental and are included for comparison only (these are most often values recommended in other compilations). Step 3. Determine the effective number of data values, ne, as described in 1.5.3. If the effective number of values is less than four, terminate the calculation. If the total number of values is more than eight and the effective number is greater than or equal to four but less than eight, make another initial data selection with relaxed selection criteria. Step 4. For the j-th value in the set calculate normalized values, ρn,j and Tn,j, and weighting factors, w j = 1 / u 2j where uj is the uncertainty assigned to the j-th observed density and

ρ n, j = ρ j − ρ

where ρ

is the mean value of the observed density in the set. and

Tn , j = T k − T k where T k is the mean value of the T jk value in the set.. Step 5. Using ρn = a1Tn , fit the data subject to least squares with points weighted by wj . Step 6. Calculate the standard deviation σ for this fit. Eliminate any points from this set for which | δj | > 3.5σ, where δ j = ρ j − ρ x , j .

Landolt-Börnstein New Series IV/8G

6

1.4 Evaluation, Selection, and Smoothing of Data Step 7. Fit the remaining normalized values to a series of polynomials, ρ n = ∑ a k T k , starting with order 1 and increasing in order. Use wj as weighting factors and stop increasing the order when satisfying one of the following conditions: 1. A value of p given as an input parameter to the program is reached, or 2. χ 2k < 11 . [1 + 1 / (n − k )]2 χ 2k − 1 (see glossary of symbols) and the deviations pass the random deviation test (see 1.5.4).

Step 8. If any points have | δj | > 2.2σ for the final polynomial, eliminate these points and repeat step 7. Step 9. Calculate parameter a0 . Step 10. Apply the initial data selection described in step 2 to the high temperature data set. Step 11. Fit the selected high temperature data with the modified Guggenheim equation using least squares with weighting factors wj . Step 12. The following procedure provides continuity at the boundary. Set equation (1.13) and its first derivative at Tb equal to the corresponding values from equation (1.12) at Tb. Eliminate parameters b3 and b4 from these two simultaneous equations to obtain a function containing parameters b1 and b2 which can be evaluated for the high temperature range using least squares. Do not use densities at temperatures within 2 K of the critical temperature. Step 13. Generate the output table of temperature, observed densities, estimated uncertainties, and difference between observed and calculated densities and arrange it in order of year of publication with authors. For data from a particular source, arrange in order of temperature. Step 14. Calculate the table of smoothed and recommended values with their corresponding estimated uncertainties. Coefficients A, B, C, D and E listed in the heading of Table 1 for each compound correspond to a0, a1, a2, a3 and a4 in equation (1.12) for temperatures below Tb. σ is the weighted standard deviation for individual points in this region (see the glossary). If the data set includes values above Tb, the coefficients A, B, C and D correspond to b1, b2, b3 and b4 in equation (1.13) for this range. The weighted standard deviation, σc,w, and the unweighted standard deviation for the fit, σc,uw, include both ranges. If the data set covers only values below Tb then σc,w and σc,uw represent that range only. The uncertainty in the smoothed values depends upon the uncertainties in the original observed values and upon the magnitude of deviations between observed and calculated values. To approximate the contribution of these two effects at the temperature T, the uncertainties ux(T) for the low temperature range are calculated from:

  u x (T ) = u(T ) 2 + ∑ ∑ Ckl (T k − T k )(T l − T l )  k l  

1/ 2

.

(1.14)

In this equation, u(T) represents the uncertainty of the observed data in the vicinity of T and is approximated by fitting a polynomial of order 1-3 to the estimated uncertainties as a function of temperature (other symbols appear in the glossary). Uncertainties in the smoothed data for the high temperature range are calculated using:

[

u x ( T ) = u x (Tb ) + h( T ) 2

−2

]

1/ 2

,

(1.15)

where ux(Tb) is the uncertainty calculated using equation (1.14) for the low temperature range at the boundary temperature Tb and h(T) is a polynomial in temperature fit to the reciprocals of the estimated uncertainties in the high temperature region. The uncertainties in extrapolated data should increase as the extent of extrapolation increases. Since equation (1.15) does not always give this result, manual adjustment is sometime required in this range.

Landolt-Börnstein New Series IV/8G

1.4 Evaluation, Selection, and Smoothing of Data -1.5 Calculation Procedures

7

1.4.4 Procedure for Selection and Smoothing of Density Values - Case 2 When the data set for a particular compound satisfies the criteria for Case 2, it is smoothed by a linear function of temperature,

ρ x = a 0 + a1T .

(1.16)

The coefficient a1 is either calculated from two densities of sufficient accuracy reported at different temperatures, preferably by the same investigator, or estimated by examination of the coefficient of expansion of similar compounds obtained from a least squares calculation. The constant term then results from equation (1.17) after eliminating values with large uncertainties

(

)

a 0 = ∑ w j ρ j − a1Tj / ∑ w j .

(1.17)

The uncertainties for the smoothed values are:

ux (T ) = [σ 20 + σ 12 (T − T ) 2 ]2 ,

(1.18)

where T is the weighted mean temperature for the accepted set, σ 20 = ( Σw jδ 2j ) / Σw j and σ1 is the estimated standard deviation of a1 .

1.4.5 Procedure for Selection and Smoothing of Density Values - Case 3 The recommended density at a particular temperature is the weighted mean observed density for that temperature. The corresponding uncertainty is the standard deviation from the mean for each value.

1.5 Calculation Procedures 1.5.1 Least Squares Calculation Parameters of all the smoothing functions are adjusted to minimize the function

χ 2 = Σw jδ 2j

(1.19)

by the singular value decomposition of the matrix of independent variables of the function. The parameters are calculated by functions svdcmp and svbksb described in [88-pre/fla] modified to accept weighting factors. The covariance matrix used in equation (1.14) is calculated by the function covar from the same book.

1.5.2 Selection of Data Based upon Estimated Uncertainties The selection procedure is: Step 1. Obtain ∆T, the range of temperatures covered by the data set. Step 2. For each density value, ρj , in the set, calculate,

(

x jl = exp q Tj − Tl z1 = ∑ x jl l≠ j

Landolt-Börnstein New Series IV/8G

)

(1.20) (1.21)

8

1.5 Calculation Procedures z2 = ∑ ul x jl

(1.22)

y = u j z11.5 z2−1

(1.23)

l≠ j

Accept point j if y ≤ d; reject it otherwise. Step 3. Repeat steps 1 and 2 with points accepted in the first pass. The accepted points are those that remain from Step 3. The constants q and d are:

[

q = −2.628 g1 1 + ( ∆T / 30)

2

] / ∆T

d = g 2 / log 10 (1 + n) . The number z2 / z1 is a weighted mean of all points in the set other than the j-th point. The weighting factor decreases exponentially with the difference in temperature of the l-th point from the j-th point. The parameter g1 determines the rate of decrease. This procedure compares the uncertainty of the j-th point to the weighted mean of other points. The parameter g2 determines the rejection level from this comparison for the j-th point. Larger values of g2 are less selective. Values for g1 and g2 are supplied to the algorithm. For all cases g1 is in the range of 1 to 2 (usually 1.8). The value of g2 is in the range of 2 to 3 (kg⋅m-3) (usually 2.5).

1.5.3 Count the Effective Number of Density Values in a Set The number of degrees of freedom in a least squares fit is the number of distinct data values minus the number of adjustable parameters. To obtain a meaningful smoothing of data, the order of the polynomial function is limited to values which gives three or more degrees of freedom. However, if two or more density values in the set are at the same (or nearly the same) temperature, they should count as only one point in calculating the degrees of freedom. In general, the effective number of density values minus the number of fitting parameters is used as the degrees of freedom. Effective data values are those that are separated by at least 1.2 K.

1.5.4 Testing a Set of Deviations between Observed and Calculated Density Values for a Random Distribution One of the criteria for acceptance of the order of a polynomial least squares fit is that the deviations between calculated and random values be distributed “randomly” over the range of conditions covered by the data. The concept of randomness for this purpose probably cannot be defined rigorously. However, the following test for randomness is used whenever the original data set contains seven or more values. Step 1. Sort the values in order of increasing temperature Step 2. Separate the total range of temperature, ∆T, into s subranges each of size ∆T/s. Form s subsets of data corresponding to these temperature subranges. Step 3. Make the following comparison for each subset j which has at least four members. 0.01 <

Σδ j ns

and

0.2 <

Σδ j Σδ j

.

If both comparisons are true for any subset, the test for randomness fails.

Landolt-Börnstein New Series IV/8G

1.5 Calculation Procedures-1.6 Glossary of Symbols

Step 4. Apply steps 2 and 3 to the data for s from 2 to an upper limit. The upper limit is determined by the number of values in the original set according to the following table.

n, number of values in original set 7 to 10 11 to 20 21 to 33 > 33

maximum number of subsets 2 3 4 5

1.6 Glossary of Symbols ak bk g1, g2 n ne ns p s uj wj Ck,l T Tb Tc Tj

parameters in the polynomial function for densities at temperatures ≤ Tb k-th parameter in modified Guggenheim equation for density at temperatures >Tb parameters used in the data selection algorithm number of accepted values of density in a set effective number of accepted values of density in a set number of density values in subset s order of the polynomial for density values at temperatures ≤ Tb number of subsets in the random deviation algorithm uncertainty assigned to the j-th observed density value in a set weighting factor for the j-th density value in a set Element k,l of the variance-covariance matrix for the polynomial parameters absolute temperature boundary temperature critical temperature temperature for the j-th observed density

Tk

mean value of the T jk values in a set

Tn,j

T jk - T k , normalized value of the j-th temperature raised to the k power

δj θj ρ ρ(API) ρ ρo ρc ρj ρm ρn,j ρr ρx,j σ χ 2k

ρj - ρx,j (1 - Tj /Tc)1/3 density API specific gravity mean value of observed densities in a set density of a standard substance critical density observed value of j-th density in a data set molar density ρj - ρ , normalized density for the j-th value relative density calculated value of the j-th density in a data set (χ2/n)1/2, standard deviation for density values in a set Σδ 2j for all values in a set fit to a polynomial of order k

∆T

Tn - T1, range of temperatures for data in a set

Landolt-Börnstein New Series IV/8G

9

10

1.6 Glossary of Symbols - 1.7 Order of Compounds in the Tables

The following symbols refer to components in a mixture at a fixed temperature c i vi wi xi Mi V Vi ρ ρi

number of components in the mixture component number partial specific volume of component i in the mixture mass fraction of component i in the mixture mole fraction of component i in the mixture molar mass (molecular weight) of component i molar volume of a mixture partial molal volume of component i in the mixture density of a mixture of components density of pure component i

Symbols used in the tables: A, B, C, D, E ρcalc ρexp σ

coefficients in function for density (see section 1.4.3) calculated density, ρx observed value of j-th density in a data set, ρj ( Σw j δ 2j / Σw j )1/ 2 , for low temperature range only

σc,w

( Σw j δ 2j / Σw j )1/ 2 , for low and high temperature range combined

σc,uw

[ Σδ 2j / n(n − p − 2)]1 / 2 , for low and high temperature range combined

2σest

estimated uncertainty, uj

1.7

Order of Compounds in the Tables

The density tables are organized into 3 main classes of compounds as described in the Table of Contents: monoalcohols, diols, and triols. Within each main class (except for the triols) there are several subclasses. They start with fully saturated compounds and proceed with increasing extents of unsaturation. Within each subclass the compounds are arranged in formula order. First with increasing number of carbon atoms in the empirical formula and then with increasing number of hydrogen atoms. Compounds with the same formula are sorted alphabetically by Table Name.

References 67-gug

Guggenheim, E.A.: Thermodynamics, 5th edition, Amsterdam: North-Holland Publishing Company (1957).

86-ros/bae

Rossiter, B.W., Baetzold, R.C.: Physical Methods of Chemistry, 2nd edition, Vol. VI, Determination of Thermodynamic Properties, New York: John Wiley & Sons (1986).

88-pre/fla

Press, W.H., Flannery, B.P., Teukolsky, S.A., Vetterling, W.T.: Numerical Recipes in C, New York: Cambridge Univ. Press (1988).

Landolt-Börnstein New Series IV/8G

2.1.1 Alkanols, C1 - C4

11

2 Tabulated Data on Density - Monoalcohols 2.1 Alkanols 2.1.1 Alkanols, C1 - C4 Methanol

[67-56-1]

CH4O

MW = 32.04

1

Tc = 512.64 K [89-tej/lee] ρc = 272.00 kg·m−3 [89-tej/lee] Table 1. Coefficients for the polynomial expansion equations. Standard deviations (see introduction): σ = 5.5832 · 10−1 (low temperature range), σc,w = (4.8307 · 10−1 combined temperature ranges, weighted), σc,uw = 3.4016 · 10−1 (combined temperature ranges, unweighted).

Coefficient

A B C D

T = 176.15 to 400.00 K T = 400.00 to 512.64 K ρ = A + BT + CT 2 + DT 3 + … ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)] [ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] 3 1.14445 · 10 2.46064 −1.79908 −5.82461 · 10−2 3.16450 · 10−3 5.61772 · 10−4 −6 −3.87839 · 10 −1.89776 · 10−6

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T Ref. (Symbol −3 −3 −3 in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m crystal 473.15 552.50 ± 3.00 −3.21 78.15 1041 ± 3.00 30-bil/fis-1 483.15 525.40 ± 3.00 −2.04 liquid 493.15 490.00 ± 3.00 2.14 296.09 789.07 ± 0.50 0.56 1887-ram/you1) 498.15 468.00 ± 3.00 6.30 296.09 789.09 ± 0.60 0.58 1887-ram/you1) 503.15 441.80 ± 5.00 12.68 353.15 736.80 ± 1.00 3.85 1887-ram/you1) 505.15 430.10 ± 5.00 16.61 363.15 723.90 ± 1.00 1.20 1887-ram/you1) 507.15 412.70 ± 5.00 17.09 373.15 713.50 ± 1.00 1.27 1887-ram/you(✕ ) 509.15 395.30 ± 5.00 21.13 383.15 702.80 ± 1.50 1.26 1887-ram/you(✕ ) 510.15 386.60 ± 5.00 25.49 393.15 689.90 ± 1.50 −0.68 1887-ram/you(✕ ) 511.15 370.50 ± 5.00 25.55 403.15 677.70 ± 1.50 −1.36 1887-ram/you(✕ ) 511.65 364.20 ± 0.00 29.63 413.15 664.90 ± 1.50 0.95 1887-ram/you(✕ ) 293.15 790.48 ± 0.00 −0.81 423.15 649.40 ± 1.50 2.71 1887-ram/you(✕ ) 343.15 745.98 ± 0.00 2.97 433.15 632.10 ± 2.00 2.92 1887-ram/you(✕ ) 353.15 735.50 ± 0.60 2.55 443.15 616.00 ± 2.00 3.84 1887-ram/you(✕ ) 363.15 725.00 ± 1.50 2.30 453.16 596.70 ± 2.00 1.43 1887-ram/you(✕ ) 373.15 714.00 ± 1.50 1.77 463.15 578.00 ± 2.00 0.76 1887-ram/you(✕ ) 383.15 702.00 ± 1.50 0.46 1)

Ref. (Symbol in Fig. 1) 1887-ram/you(✕ ) 1887-ram/you(✕ ) 1887-ram/you(✕ ) 1887-ram/you(✕ ) 1887-ram/you1) 1887-ram/you1) 1887-ram/you1) 1887-ram/you1) 1887-ram/you1) 1887-ram/you1) 1887-ram/you1) 1893-ram/shi-31) 1893-ram/shi-31) 1893-ram/shi-31) 1893-ram/shi-31) 1893-ram/shi-3(✕ ) 1893-ram/shi-3(✕ )

Not included in Fig. 1.

cont.

Landolt-Börnstein New Series IV/8G

12

2.1.1 Alkanols, C1 - C4

Methanol (cont.) Table 2. (cont.) ρexp ± 2σ est T K kg ⋅ m−3 393.15 690.00 ± 1.50 403.15 677.00 ± 1.50 413.15 664.00 ± 1.50 423.15 649.50 ± 1.50 433.15 634.00 ± 2.00 443.15 616.00 ± 2.00 453.15 598.00 ± 2.00 463.15 577.00 ± 2.00 473.15 553.00 ± 3.00 483.15 525.50 ± 3.00 493.15 490.00 ± 3.00 503.15 441.00 ± 5.00 507.15 414.50 ± 5.00 509.15 395.50 ± 5.00 513.15 271.20 ± 0.00 293.15 791.31 ± 0.06 323.15 763.20 ± 0.40 333.15 753.60 ± 0.40 343.15 744.20 ± 0.40 353.15 734.70 ± 0.50 363.15 725.10 ± 0.60 403.15 671.80 ± 1.00 413.15 657.40 ± 1.00 423.15 642.00 ± 1.00 433.15 625.80 ± 1.50 443.15 608.10 ± 1.50 453.15 589.10 ± 1.50 463.15 568.10 ± 2.00 473.15 544.80 ± 2.00 483.15 517.00 ± 2.00 493.15 481.10 ± 3.00 503.15 432.10 ± 5.00 512.58 272.00 ± 5.00 283.15 800.45 ± 0.10 288.15 795.81 ± 0.10 293.15 791.32 ± 0.10 273.15 809.98 ± 0.10 176.15 904.60 ± 0.70 183.15 897.00 ± 0.70 193.15 886.80 ± 0.60 203.15 876.50 ± 0.60 213.15 866.60 ± 0.60 1)

ρexp − ρcalc kg ⋅ m

Ref. (Symbol in Fig. 1)

−0.58 −2.06 0.05 2.81 4.82 3.84 2.71 −0.24 −2.71 −1.94 2.14 11.88 18.89 21.33 19.30 0.02 0.55 0.70 1.19 1.75 2.40 −7.26 −6.55 −4.69 −3.38 −4.06 −6.19 −9.14 −10.91 −10.44 −6.76 2.98 −23.47 −0.25 −0.19 0.03 −0.11 0.07 −0.27 −0.26 −0.55 −0.59

1893-ram/shi-3(✕ ) 1893-ram/shi-3(✕ ) 1893-ram/shi-3(✕ ) 1893-ram/shi-3(✕ ) 1893-ram/shi-3(✕ ) 1893-ram/shi-3(✕ ) 1893-ram/shi-3(✕ ) 1893-ram/shi-3(✕ ) 1893-ram/shi-3(✕ ) 1893-ram/shi-3(✕ ) 1893-ram/shi-3(✕ ) 1893-ram/shi-31) 1893-ram/shi-31) 1893-ram/shi-31) 1893-ram/shi-31) 32-ros(∇) 50-hou/mas-11) 50-hou/mas-11) 50-hou/mas-1(✕ ) 50-hou/mas-1(✕ ) 50-hou/mas-11) 55-kay/don(✕ ) 55-kay/don(✕ ) 55-kay/don(✕ ) 55-kay/don(✕ ) 55-kay/don(✕ ) 55-kay/don(✕ ) 55-kay/don(✕ ) 55-kay/don(✕ ) 55-kay/don(✕ ) 55-kay/don(✕ ) 55-kay/don1) 55-kay/don1) 58-yam/kun(✕ ) 58-yam/kun(✕ ) 58-yam/kun1) 59-mck/ski(✕ ) 67-kom/man(✕ ) 67-kom/man1) 67-kom/man1) 67-kom/man1) 67-kom/man1)

−3

T K

223.15 233.15 243.15 253.15 263.15 273.15 283.15 293.15 298.15 413.15 423.15 433.15 443.15 453.15 463.15 473.15 483.15 493.15 498.15 503.15 505.15 507.15 509.15 511.15 512.65 183.15 193.15 203.15 213.15 223.15 233.15 243.15 253.15 263.15 273.15 283.15 281.40 284.78 285.69 288.72 289.64 292.96

ρexp ± 2σ est kg ⋅ m

−3

ρexp − ρcalc −3

kg ⋅ m

857.20 ± 0.50 −0.26 847.80 ± 0.50 −0.06 0.06 838.40 ± 0.50 0.11 829.00 ± 0.40 0.12 819.60 ± 0.40 0.11 810.20 ± 0.40 0.10 800.80 ± 0.40 0.01 791.30 ± 0.40 0.44 787.00 ± 0.40 636.94 ± 0.00 −27.01 628.93 ± 0.00 −17.76 621.12 ± 0.00 −8.06 609.76 ± 0.00 −2.40 594.11 ± 1.50 −1.18 573.39 ± 1.50 −3.85 550.99 ± 1.50 −4.72 524.49 ± 1.50 −2.95 1.14 489.00 ± 2.00 5.20 466.90 ± 2.00 440.01 ± 2.00 10.89 426.20 ± 2.00 12.71 409.70 ± 3.00 14.09 387.81 ± 3.00 13.64 1.92 346.87 ± 3.00 2.05 274.57 ± 0.00 896.80 ± 0.20 −0.47 886.70 ± 0.20 −0.36 876.80 ± 0.20 −0.25 0.11 867.30 ± 0.20 857.40 ± 0.20 −0.06 0.04 847.90 ± 0.20 838.30 ± 0.20 −0.04 0.01 828.90 ± 0.20 0.22 819.70 ± 0.20 0.31 810.40 ± 0.20 0.10 800.80 ± 0.20 802.32 ± 0.20 −0.03 798.99 ± 0.20 −0.18 798.15 ± 0.20 −0.16 795.35 ± 0.20 −0.11 794.49 ± 0.20 −0.11 791.41 ± 0.20 −0.06

Ref. (Symbol in Fig. 1) 67-kom/man1) 67-kom/man1) 67-kom/man1) 67-kom/man1) 67-kom/man1) 67-kom/man1) 67-kom/man1) 67-kom/man1) 67-kom/man1) 69-zub/bag1) 69-zub/bag1) 69-zub/bag1) 69-zub/bag1) 69-zub/bag(✕ ) 69-zub/bag(✕ ) 69-zub/bag(✕ ) 69-zub/bag(✕ ) 69-zub/bag(✕ ) 69-zub/bag(✕ ) 69-zub/bag(✕ ) 69-zub/bag(✕ ) 69-zub/bag(✕ ) 69-zub/bag(✕ ) 69-zub/bag(✕ ) 69-zub/bag1) 71-yer/swi(✕ ) 71-yer/swi(✕ ) 71-yer/swi(✕ ) 71-yer/swi(✕ ) 71-yer/swi(✕ ) 71-yer/swi(✕ ) 71-yer/swi(✕ ) 71-yer/swi(✕ ) 71-yer/swi(✕ ) 71-yer/swi1) 71-yer/swi1) 72-rei/eis( ) 72-rei/eis( ) 72-rei/eis( ) 72-rei/eis( ) 72-rei/eis( ) 72-rei/eis( )

Not included in Fig. 1.

cont.

Landolt-Börnstein New Series IV/8G

2.1.1 Alkanols, C1 - C4 Table 2. (cont.) ρexp − ρcalc ρexp ± 2σ est T −3 kg ⋅ m−3 K kg ⋅ m 293.82 790.60 ± 0.20 −0.06 296.97 787.67 ± 0.20 −0.01 297.87 786.82 ± 0.20 −0.01 300.90 783.98 ± 0.20 0.02 301.62 783.29 ± 0.20 0.02 304.83 780.27 ± 0.20 0.04 305.70 779.45 ± 0.20 0.05 308.32 776.96 ± 0.20 0.06 309.17 776.16 ± 0.20 0.07 311.32 774.13 ± 0.20 0.09 312.17 773.33 ± 0.20 0.11 317.16 768.56 ± 0.20 0.12 293.15 791.04 ± 0.20 −0.25 298.15 786.37 ± 0.20 −0.19 303.15 781.65 ± 0.20 −0.17 320.00 765.59 ± 0.20 −0.11 340.00 745.88 ± 0.20 −0.26 360.00 725.21 ± 0.20 −0.74 380.00 703.03 ± 0.25 −1.90 400.00 678.69 ± 0.25 −4.23 410.00 665.40 ± 0.25 −3.66 420.00 651.27 ± 0.20 −0.95 430.00 636.05 ± 0.30 1.40 440.00 619.50 ± 0.30 2.03 293.15 791.25 ± 0.05 −0.04 298.15 786.57 ± 0.03 0.01 298.15 786.55 ± 0.06 −0.01 298.15 786.57 ± 0.05 0.01 273.15 809.99 ± 0.20 −0.10 283.15 800.70 ± 0.20 −0.00 293.15 791.32 ± 0.20 0.03 303.15 781.86 ± 0.20 0.04 313.15 772.32 ± 0.20 0.03 1)

Ref. (Symbol in Fig. 1)

72-rei/eis( ) 72-rei/eis( ) 72-rei/eis( ) 72-rei/eis( ) 72-rei/eis( ) 72-rei/eis( ) 72-rei/eis( ) 72-rei/eis( ) 72-rei/eis( ) 72-rei/eis( ) 72-rei/eis( ) 72-rei/eis( ) 76-hal/ell1) 76-hal/ell1) 76-hal/ell1) 76-hal/ell1) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell1) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 84-cer/bou( ) 86-oga/mur( ) 86-tan/toy(◆) 87-oga/mur(∆) 88-sun/bis1) 88-sun/bis1) 88-sun/bis1) 88-sun/bis1) 88-sun/bis1)

T K

323.15 333.15 205.16 212.69 223.11 232.45 243.17 252.11 261.62 269.38 273.27 281.82 292.38 294.36 298.16 303.14 313.14 323.17 333.15 203.15 213.15 223.15 233.15 243.15 253.15 263.15 298.15 303.15 308.15 298.15 303.15 308.15

13

ρexp ± 2σ est

ρexp − ρcalc

−3

kg ⋅ m

kg ⋅ m−3

Ref. (Symbol in Fig. 1)

762.70 ± 0.20 753.00 ± 0.20 875.03 ± 0.20 867.57 ± 0.20 857.33 ± 0.20 848.35 ± 0.20 838.12 ± 0.20 829.73 ± 0.20 820.74 ± 0.20 813.50 ± 0.20 809.79 ± 0.20 801.87 ± 0.20 792.04 ± 0.20 790.05 ± 0.20 786.55 ± 0.20 781.79 ± 0.20 772.23 ± 0.20 762.58 ± 0.20 752.62 ± 0.20 877.08 ± 0.20 867.09 ± 0.20 857.29 ± 0.20 847.65 ± 0.20 838.13 ± 0.20 828.70 ± 0.20 819.33 ± 0.20 786.80 ± 0.20 781.80 ± 0.20 777.10 ± 0.20 786.60 ± 0.20 781.70 ± 0.20 776.90 ± 0.20

0.05 0.10 −0.02 −0.07 −0.17 −0.18 −0.20 −0.14 −0.18 −0.13 −0.19 −0.08 0.03 −0.10 −0.00 −0.04 −0.06 −0.05 −0.28 0.03 −0.10 −0.17 −0.21 −0.21 −0.19 −0.15 0.24 −0.02 0.04 0.04 −0.12 −0.16

88-sun/bis(✕ ) 88-sun/bis(✕ ) 88-sun/sch-1(✕ ) 88-sun/sch-1(✕ ) 88-sun/sch-1(✕ ) 88-sun/sch-1(✕ ) 88-sun/sch-1(✕ ) 88-sun/sch-1(✕ ) 88-sun/sch-1(✕ ) 88-sun/sch-1(✕ ) 88-sun/sch-11) 88-sun/sch-11) 88-sun/sch-11) 88-sun/sch-11) 88-sun/sch-11) 88-sun/sch-11) 88-sun/sch-11) 88-sun/sch-1(✕ ) 88-sun/sch-1(✕ ) 90-sun/sch-1(✕ ) 90-sun/sch-1(✕ ) 90-sun/sch-1(✕ ) 90-sun/sch-1(✕ ) 90-sun/sch-1(✕ ) 90-sun/sch-1(✕ ) 90-sun/sch-1(✕ ) 98-ami/ban( ) 98-ami/ban( ) 98-ami/ban( ) 98-ami/pat-1(∆) 98-ami/pat-1(∆) 98-ami/pat-1(∆)

Not included in Fig. 1.

Further references: [1848-kop, 1854-kop, 1863-gla/dal, 1864-lan, 1880-pry, 1882-sch-1, 1883-sch-3, 1884-gla, 1884-per, 1884-sch-6, 1884-zan, 1886-tra, 1890-gar, 1891-jah, 1891-sch/kos, 1892-lan/jah, 1896-zel/kra, 1898-kah, 1898-roh, 00-loo, 02-you/for, 03-car/cop, 04-bru/sch, 04-cri, 06-car/fer, 06-kla/nor, 06-wal-1, 07-che-1, 07-tim, 08-get, 08-gyr, 08-ric/mat, 09-dor, 09-hol/sag, 10-daw, 10-dor/pol, 10-fon, 10-tim, 11-dor, 12-kor, 12-mal, 12-tim, 12-tim-1, 12-tyr, 13-atk/wal, 13-bri-1, 13-rom, 13-ste, 14-kre/mei, 14-low, 14-mer/tur, 14-tyr, 15-ric/coo, 16-har-2, 16-ric/shi, 16-sei/alt, 16-wro/rei, 17-jae, 18-her-2, 19-eyk, 20-ric/dav, 21-bar/bir, 21-rei/hic, 22-her/sch, 22-mck/sim, 23-wil/smi, 24-bus-1, 24-dan, 24-mar-1, 24-mil, 25-har/rai, 25-lew, 25-nor/ash, 25-par, 25-per, 25-rak, 26-ewa/rai, 26-gol/aar, 26-mat, 26-mun, 26-ris/hic, 26-sch, 27-arb-2, 28-llo/bro, 29-kel-1, 30-bil/fis-1, 30-rak/fro, 30-tim/hen, 31-bea/mcv, 31-fio/gin, 31-lun/bje, 33-but/tho, 33-koz/koz, 33-nat/bac, 33-vos/con, 34-cor/arc, 34-smi, 34-was/spe, 35-gib, 35-hen, 35-kef/mcl, 36-tom] cont.

Landolt-Börnstein New Series IV/8G

14

2.1.1 Alkanols, C1 - C4

Methanol (cont.) Further references: (cont.) [37-bet/ham, 37-gib/kin, 37-sta/gil, 38-jon/for, 39-lar/hun, 40-pes-1, 40-was/gra, 42-bri/rin, 42-mor/mun, 42-mul, 43-eck/luc, 44-pes/lag, 45-add, 45-dul, 46-kre/now, 46-sca/woo, 46-sca/woo-1, 47-woo, 48-jon/bow, 48-vog-2, 48-wei, 48-wil/ros, 49-gor/gor, 49-gri/buf, 49-hat, 49-sta/gup, 49-tsc/ric, 49-udo/kal, 50-jac, 50-joe/nik, 50-lar/ver, 50-pic/zie, 50-sac/sau, 50-sad/fuo, 50-tei/gor, 50-wol/sau, 51-car/rid, 51-cli/cam, 51-lyu/ter, 51-sie/cru, 51-tei/gor, 52-hug/mal, 52-sca/tic, 52-sta/spi, 53-ame/pax, 53-ani-1, 53-mck/tar, 53-par/cha, 54-col, 54-cro/spi, 54-gri, 54-kre/wie, 54-pur/bow, 54-sad/fuo, 55-den/col, 55-gre/ven, 55-ham/sto, 56-ame/pax, 56-fai/win, 57-gol, 57-mil, 57-tul/chr, 58-ano-5, 58-cos/bow, 58-lin/van, 58-mur/van, 59-ale, 59-yen/ree, 60-cop/fin, 61-mik/kim, 62-bro/smi, 62-chu/tho, 62-mik/kim, 62-nag-4, 62-par/mis, 63-aki/yos, 63-fis, 63-hov/sea, 63-mcc/lai, 63-raj/ran, 64-ma /koh, 65-for/moo, 66-kat/pra-1, 66-kat/shi, 67-cun/vid, 67-fre, 67-han/hac, 67-nak/nak, 67-nak/shi, 67-sum/tho, 68-ano, 68-bek/hal, 68-nak/shi, 68-pfl/pop, 68-sin/ben, 69-bru/gub, 70-iin/sud, 70-kat/kon, 70-kat/kon-1, 70-kon/lya, 70-nak/shi, 70-str/svo, 71-des/bha, 71-des/bha-1, 71-nag/oht, 72-bou/aim, 72-nie/nov, 72-pol/lu, 72-pol/lu -1, 73-khi/ale, 73-svo/ves, 74-dut/mat, 75-mat/fer, 75-mus/ver, 75-nak/wad, 75-tok, 76-kat/nit, 76-mcg/wil, 76-nag/oht, 76-nak/ash, 76-sri/kul, 76-wes, 77-hwa/rob, 77-sch/pla, 77-tre/ben, 78-och/lu, 79-cha/ses-1, 79-cib/hyn, 79-coc/pis, 79-dia/tar, 79-jim/paz, 79-kiy/ben, 80-aim/cip, 80-arc/bla, 80-ben/kiy, 80-edu/boy, 80-kub/tsu, 80-yos/tak, 81-fre/cri, 81-kum/pra, 81-sjo/dyh, 81-tas/ara, 81-won/chu, 82-diz/mar, 82-dom/rat, 82-ort, 83-fuk/ogi, 83-pik-2, 83-rau/ste, 83-tri, 84-sak/nak, 85-dri/ras, 85-kov/svo, 85-mat/ben, 85-mat/ben-1, 85-nag, 85-ort/paz-1, 85-pat/san, 85-sch/pla, 85-tri/rod, 86-bot/bre, 86-cra, 86-hne/cib, 86-kud/str, 86-lep/mat, 86-lin/ber, 86-miy/hay, 86-san/sha, 86-yer/wor, 86-zha/ben-1, 87-ham/als, 87-kub/tan, 87-lin/ber, 87-man/ami, 87-pik, 88-aww/all, 88-bag/gur, 88-ben/van, 88-man/ami, 88-nag-2, 88-ohg/tak, 88-oka/oga, 89-ala/sal, 89-ale/fer, 89-dou/kha, 89-kat/tan, 89-kat/tan-1, 89-nao/sur, 89-raj/ren, 90-arc/dom, 90-cha/kat, 90-jos/ami-1, 90-lee/hon, 90-let/sch-1, 90-rie/sch, 91-cab/bel, 91-gar/her, 91-kat/tan, 91-liu/pus, 91-ram/muk, 92-hia/yam, 92-lee/wei, 92-pap/zio, 92-pla/ste, 93-ami/ara, 94-arc/bla, 94-kim/lee, 94-pap/pan-1, 95-arc/bla, 95-che/kna, 95-red/ram-1, 96-nik/jad, 96-nik/mah, 97-arc/bla, 97-com/fra, 98-arc/mar, 98-arc/nar, 98-bla/ort, 98-igl/org, 98-nik/shi, 98-zie]. Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

170.00 180.00 190.00 200.00 210.00 220.00 230.00 240.00 250.00 260.00 270.00 280.00 290.00

ρ ± σ fit kg ⋅ m−3 911.00 ± 0.33 900.52 ± 0.33 890.26 ± 0.32 880.18 ± 0.31 870.28 ± 0.29 860.51 ± 0.26 850.87 ± 0.23 841.33 ± 0.19 831.86 ± 0.15 822.44 ± 0.12 813.05 ± 0.09 803.66 ± 0.07 794.26 ± 0.06

T K

293.15 298.15 300.00 310.00 320.00 330.00 340.00 350.00 360.00 370.00 380.00 390.00 400.00

ρ ± σ fit kg ⋅ m−3 791.29 ± 0.06 786.56 ± 0.07 784.81 ± 0.07 775.30 ± 0.10 765.70 ± 0.15 755.99 ± 0.23 746.14 ± 0.34 736.13 ± 0.47 725.95 ± 0.64 715.55 ± 0.85 704.93 ± 1.11 694.06 ± 1.40 682.92 ± 1.75

T K

410.00 420.00 430.00 440.00 450.00 460.00 470.00 480.00 490.00 500.00 510.00

ρ ± σ fit kg ⋅ m−3 669.06 ± 1.88 652.22 ± 1.91 634.65 ± 1.94 617.47 ± 1.99 600.65 ± 2.05 583.17 ± 2.14 563.04 ± 2.29 537.31 ± 2.83 501.91 ± 3.95 450.53 ± 4.84 363.22 ± 6.34

cont.

Landolt-Börnstein New Series IV/8G

15

ρ

ρ

2.1.1 Alkanols, C1 - C4

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Ethanol

[64-17-5]

C2H6O

MW = 46.07

2

Tc = 514.10 K [89-tej/lee] ρc = 276.00 kg·m−3 [89-tej/lee] Table 1. Coefficients for the polynomial expansion equations. Standard deviations (see introduction): σ = 2.7027 · 10−1 (low temperature range), σc,w = (1.5405 · 10−1 combined temperature ranges, weighted), σc,uw = 1.5778 · 10−1 (combined temperature ranges, unweighted).

Coefficient

A B C D

T = 191.15 to 400.00 K ρ = A + BT + CT 2 + DT 3 + …

1.16239 · 103 −2.25788 5.30621 · 10−3 −6.63070 · 10−6

T = 400.00 to 514.10 K ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)] [ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] 1.73318 −3.58319 · 10−2 3.19777 · 10−4 −1.03287 · 10−6

cont.

Landolt-Börnstein New Series IV/8G

16

2.1.1 Alkanols, C1 - C4

Ethanol (cont.) Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m crystal 298.15 784.96 ± 0.05 −0.19 78.15 1021 ± 3.0 30-bilfis-1 303.15 780.67 ± 0.05 −0.15 liquid 308.15 776.38 ± 0.05 −0.08 288.15 793.75 ± 0.08 0.03 13-osb/mck(✕ ) 223.15 848.91 ± 0.10 −0.18 298.15 785.03 ± 0.08 −0.12 13-osb/mck1) 223.17 848.99 ± 0.10 −0.08 273.15 806.28 ± 0.08 −0.14 48-kre/now(◆) 233.15 840.29 ± 0.10 −0.08 298.15 785.04 ± 0.08 −0.11 48-kre/now1) 233.15 840.31 ± 0.10 −0.06 353.15 763.12 ± 0.08 28.38 48-kre/now1) 233.15 840.39 ± 0.10 0.02 273.15 806.30 ± 0.40 −0.12 58-cos/bow1) 233.15 840.28 ± 0.10 −0.09 293.15 789.40 ± 0.40 −0.05 58-cos/bow1) 243.13 831.74 ± 0.10 −0.06 1) 313.15 772.20 ± 0.40 0.14 58-cos/bow 243.15 831.79 ± 0.10 0.01 333.15 754.10 ± 0.40 0.17 58-cos/bow1) 243.15 831.71 ± 0.10 −0.07 353.15 734.80 ± 0.50 0.06 58-cos/bow1) 243.15 831.73 ± 0.10 −0.05 373.15 715.70 ± 0.50 1.51 58-cos/bow1) 253.14 823.28 ± 0.10 −0.01 393.15 692.50 ± 0.50 0.57 58-cos/bow(✕ ) 253.14 823.26 ± 0.10 −0.03 413.15 663.10 ± 0.60 −2.49 58-cos/bow(✕ ) 253.18 823.25 ± 0.10 −0.01 433.15 632.90 ± 0.60 −0.00 58-cos/bow(✕ ) 258.15 819.03 ± 0.10 −0.03 453.15 598.40 ± 0.60 0.81 58-cos/bow(✕ ) 258.15 819.04 ± 0.10 −0.02 473.15 556.80 ± 0.70 2.22 58-cos/bow(✕ ) 263.15 814.83 ± 0.10 −0.01 483.15 518.60 ± 2.00 −7.37 64-ska/kay(✕ ) 263.15 814.82 ± 0.10 −0.02 488.15 503.40 ± 2.00 −5.29 64-ska/kay(✕ ) 268.15 810.62 ± 0.10 −0.01 493.15 486.30 ± 2.00 −2.43 64-ska/kay(✕ ) 268.15 810.60 ± 0.10 −0.03 498.15 466.80 ± 2.00 1.52 64-ska/kay(✕ ) 273.14 806.30 ± 0.10 −0.12 503.15 443.20 ± 3.00 6.26 64-ska/kay(✕ ) 273.15 806.32 ± 0.10 −0.10 508.15 411.30 ± 3.00 10.86 64-ska/kay1) 283.15 797.88 ± 0.10 −0.08 513.15 339.50 ± 5.00 1.88 64-ska/kay(✕ ) 283.15 797.89 ± 0.10 −0.07 293.15 789.20 ± 0.20 −0.25 76-hal/ell1) 293.17 789.28 ± 0.10 −0.15 298.15 784.93 ± 0.20 −0.22 76-hal/ell1) 293.18 789.26 ± 0.10 −0.16 303.15 780.64 ± 0.20 −0.18 76-hal/ell1) 298.15 785.27 ± 0.02 0.12 320.00 765.83 ± 0.20 −0.12 76-hal/ell(✕ ) 298.15 785.10 ± 0.02 −0.05 340.00 747.47 ± 0.20 −0.02 76-hal/ell(✕ ) 303.15 780.74 ± 0.15 −0.08 360.00 727.80 ± 0.20 −0.07 76-hal/ell(✕ ) 333.15 754.38 ± 0.15 0.45 380.00 706.17 ± 0.20 −0.60 76-hal/ell(✕ ) 298.15 784.50 ± 0.08 −0.65 400.00 681.96 ± 0.30 −1.90 76-hal/ell1) 308.15 776.30 ± 0.08 −0.16 420.00 654.27 ± 0.30 −0.49 76-hal/ell(✕ ) 191.15 878.08 ± 0.20 −0.28 430.00 638.82 ± 0.50 0.60 76-hal/ell(✕ ) 202.34 867.78 ± 0.20 −0.06 440.00 621.92 ± 0.50 0.76 76-hal/ell(✕ ) 212.98 858.24 ± 0.20 0.10 450.00 603.52 ± 0.50 0.09 76-hal/ell(✕ ) 222.18 850.13 ± 0.20 0.19 455.00 593.63 ± 0.50 −0.46 76-hal/ell(✕ ) 229.95 843.37 ± 0.20 0.23 298.15 785.13 ± 0.02 −0.02 239.35 835.28 ± 0.20 0.25 79-kiy/ben(∆) 288.15 793.50 ± 0.05 −0.22 0.02 80-ben/kiy(∇) 250.85 825.25 ± 0.20 293.15 789.24 ± 0.05 −0.21 0.27 80-ben/kiy(∇) 260.49 817.35 ± 0.20 1)

Ref. (Symbol in Fig. 1) 80-ben/kiy1) 80-ben/kiy(∇) 80-ben/kiy(∇) 82-sch/pol(✕ ) 82-sch/pol(✕ ) 82-sch/pol1) 82-sch/pol1) 82-sch/pol1) 82-sch/pol1) 82-sch/pol1) 82-sch/pol1) 82-sch/pol1) 82-sch/pol1) 82-sch/pol(✕ ) 82-sch/pol(✕ ) 82-sch/pol(✕ ) 82-sch/pol(✕ ) 82-sch/pol(✕ ) 82-sch/pol(✕ ) 82-sch/pol(✕ ) 82-sch/pol(✕ ) 82-sch/pol(✕ ) 82-sch/pol1) 82-sch/pol1) 82-sch/pol(✕ ) 82-sch/pol(✕ ) 82-sch/pol1) 82-sch/pol1) 84-eas/woo( ) 86-oga/mur( ) 87-pik1) 87-pik(✕ ) 87-rat/sin-31) 87-rat/sin-3(✕ ) 88-sun/sch-1(✕ ) 88-sun/sch-1(✕ ) 88-sun/sch-1(✕ ) 88-sun/sch-11) 88-sun/sch-11) 88-sun/sch-11) 88-sun/sch-11) 88-sun/sch-11)

Not included in Fig. 1.

cont.

Landolt-Börnstein New Series IV/8G

2.1.1 Alkanols, C1 - C4 Table 2. (cont.) ρexp − ρcalc ρexp ± 2σ est T −3 kg ⋅ m−3 K kg ⋅ m 268.58 810.46 ± 0.20 0.19 280.78 800.14 ± 0.20 0.17 292.39 790.25 ± 0.20 0.15 298.15 785.31 ± 0.20 0.16 303.15 780.93 ± 0.20 0.11 313.17 772.17 ± 0.20 0.13 323.21 763.20 ± 0.20 0.15 333.15 754.15 ± 0.20 0.22 273.15 806.27 ± 0.20 −0.15 283.15 797.83 ± 0.20 −0.13 293.15 789.34 ± 0.20 −0.11 303.15 780.81 ± 0.20 −0.01 313.15 772.23 ± 0.20 0.17 323.15 763.61 ± 0.20 0.50 333.15 754.94 ± 0.20 1.01 193.15 876.24 ± 0.10 −0.22 1)

Ref. (Symbol in Fig. 1) 88-sun/sch-11) 88-sun/sch-11) 88-sun/sch-11) 88-sun/sch-11) 88-sun/sch-11) 88-sun/sch-11) 88-sun/sch-1(✕ ) 88-sun/sch-1(✕ ) 88-sun/ten1) 88-sun/ten1) 88-sun/ten1) 88-sun/ten1) 88-sun/ten1) 88-sun/ten(✕ ) 88-sun/ten(✕ ) 91-sun/sch(✕ )

T K

203.15 213.15 223.15 233.15 243.15 253.15 263.15 320.00 380.00 400.00 420.00 420.00 440.00 460.00 480.00

17

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m

kg ⋅ m−3

−3

867.05 ± 0.10 858.06 ± 0.10 849.24 ± 0.10 840.57 ± 0.10 832.00 ± 0.10 823.50 ± 0.10 815.04 ± 0.10 766.04 ± 0.20 705.92 ± 0.20 681.80 ± 0.20 654.35 ± 0.30 654.24 ± 0.20 622.02 ± 0.30 582.79 ± 0.50 535.76 ± 1.00

−0.04 0.07 0.15 0.20 0.22 0.22 0.20 0.09 −0.85 −2.06 −0.41 −0.52 0.86 −1.47 0.02

Ref. (Symbol in Fig. 1) 91-sun/sch(✕ ) 91-sun/sch(✕ ) 91-sun/sch(✕ ) 91-sun/sch1) 91-sun/sch1) 91-sun/sch(✕ ) 91-sun/sch(✕ ) 96-tak/uem(✕ ) 96-tak/uem(✕ ) 96-tak/uem1) 96-tak/uem(✕ ) 96-tak/uem(✕ ) 96-tak/uem(✕ ) 96-tak/uem(✕ ) 96-tak/uem(✕ )

Not included in Fig. 1.

Further references: [94-gil, 1811-bra, 1864-lan, 1865-men, 1869-dup/pag, 1882-sch-1, 1883-sch-3, 1884-per, 1884-sch-6, 1888-ket, 1890-gar, 1891-jah, 1891-sch/kos, 1892-lan/jah, 1893-eyk, 1897-zec, 1898-kah, 1898-roh, 00-loo, 01-rud, 02-you, 03-car/cop, 04-bru/sch, 04-cri, 04-dun, 05-win, 06-kla/nor, 06-wal-1, 07-che, 07-dun/tho, 07-tim, 08-and, 08-dor/rak, 08-dun/stu, 08-get, 08-ric/mat, 09-hol/sag, 10-daw, 10-dor/pol, 10-pol, 10-tho, 11-del, 11-dor, 11-kai, 12-kor, 12-mal, 12-osb/mck, 12-sch-1, 12-tyr, 12-wad/mer, 12-wre, 13-bri-1, 13-mer, 13-muc, 13-rob/acr, 13-rom, 13-ste, 14-low, 14-mer/tur, 14-tyr, 15-pea, 15-pri, 15-ric/coo, 16-ric/shi, 16-sei/alt, 16-wro/rei, 17-jae, 18-her-2, 19-eyk, 21-bar/bir, 21-bru/cre, 21-rei/hic, 22-her/sch, 22-mck/sim, 22-sch/reg, 22-tro, 23-moe-1, 23-rii, 23-wil/smi, 24-par/sch, 25-gro/kel, 25-nor/ash, 25-pal/con, 25-par/kel-1, 25-per, 25-rak, 25-ric/cha, 26-bar, 26-gol/aar, 26-mat, 26-mun, 26-sch, 27-arb-2, 27-del, 27-krc/wil, 28-llo/bro, 28-mon, 28-par/nel, 29-ber/reu, 29-ham/and, 29-kel-3, 29-smy/sto, 30-bil/fis-1, 30-fro, 30-mon, 31-bea/mcv, 31-fio/gin, 31-lun/bje, 32-ess/cla, 32-ros, 32-sol/mol, 32-swi/zma, 33-har, 33-vos/con, 34-lal, 35-hen, 36-tom, 37-dol/bri, 37-zep, 38-sca/ray, 39-lar/hun, 40-gos-1, 40-mon/qui, 40-tri/ric, 40-was/gra, 42-mul, 43-bru/bog, 45-add, 45-dul, 46-kre/now, 47-rei/dem, 47-sho/pri, 48-jon/bow, 48-vog-2, 48-wei, 48-zas, 49-dre/mar, 49-gri/chu, 49-hat, 49-hat-1, 49-hat-2, 49-kre/wie-1, 49-tsc/ric, 49-tsv/mar, 49-vve/iva, 50-jac, 50-pic/zie, 50-sac/sau, 50-tei/gor, 50-vie, 50-wol/sau, 51-tei/gor, 52-gri, 52-hug/mal, 52-kip/tes, 52-sta/spi, 53-ame/pax, 53-ani, 53-ani-1, 53-bar-5, 53-bar/bro, 53-cha/mou, 53-kha/kud, 53-mck/tar, 53-ots/wil, 54-gri, 54-pur/bow, 54-smi/otv, 54-tha/row, 55-fle/sau, 55-ham/sto, 56-ame/pax, 56-fai/win, 56-kat/new, 58-ano-5, 58-lin/van, 58-muk/gru, 58-mur/van, 58-oga/tak, 58-wag/web, 59-bar/dod, 59-mck/ski, 59-nie/web, 60-cop/fin, 60-fro/shr, 60-oak/web, 61-bel/web, 62-bro/smi, 62-kae/web, 63-aga/men, 63-hov/sea, 63-kud/sus-1, 63-mcc/lai, 64-sca/sat, 67-kom/man, 67-mis/sub, 68-ano, 68-kaw/min, 68-pfl/pop, 68-sin/ben, 69-fin/cop, 70-kat/kon, 70-kon/lya, 70-min/kaw, 70-nak/shi, 70-sus/hol, 71-bra/joh, 71-nag/oht, 72-nie/nov, 72-pol/lu, 72-pol/lu -1, 73-khi/ale, 74-dut/mat, 74-mye/cle, 75-mat/fer, 75-mus/ver, 75-tok, 76-for/ben, 76-kat/nit, 76-nag/oht, 76-wes, 77-gup/han, 77-hwa/rob, 77-tan/yam, 77-tre/ben, 78-nit/fuj, 79-cha/ses-1, 79-dia/tar, 79-jim/paz, 79-tho/nag, 80-arc/bla, 80-edu/boy, 80-fuk/ogi, 80-mar/ric, 80-oza/ooy, 80-pik, 80-yos/tak, 80-yu /ish, 81-kum/pra, 81-oht/koy, 81-sjo/dyh, 81-tas/ara, 81-won/chu, 82-diz/mar, 82-dom/rat, 82-ort, 83-alb/edg, 83-fuk/ogi, 83-pik-1, 83-pik-2, 83-rau/ste, 83-tri, 84-sak/nak, 85-dri/ras, 85-kov/svo, 85-mat/ben, 85-mat/ben-1, 85-nag, 85-nag-3, 85-ogi/ara, 85-ort/paz-1, 86-lep/mat, 86-miy/hay, 86-ort/pen, 86-san/sha, 86-tan/toy, 86-zha/ben-1, 87-ber-1, 87-ber-8, 87-ber-9, 87-kub/tan, 87-mou, 87-oga/mur, 87-ogi/ara, 87-pap/pap, 88-nag-4, 89-ala/sal, 89-kac/rad]

cont.

Landolt-Börnstein New Series IV/8G

18

2.1.1 Alkanols, C1 - C4

Ethanol (cont.) Further references: (cont.) 90-cha/kat, 91-pap/zio, 94-pap/pan, 97-com/fra,

ρ

ρ

[89-kat/tan, 89-kat/tan-1, 89-kou/pan, 89-nao/sur, 89-ort/sus, 89-sol/mar, 89-sus/ort, 90-let/sch-1, 90-siv/rao, 91-cab/bel, 91-gar/her, 91-kat/tan, 91-pap/eva, 91-pap/zia, 91-ram/muk, 91-vro/noo, 92-hia/yam, 92-lee/wei, 93-ami/ara, 94-hia/tak-1, 94-kim/lee, 94-pap/pan-1, 94-sol/bar, 95-arc/bla, 95-hia/tak-1, 96-elb, 96-nik/jad, 96-nik/mah, 98-ami/ban, 98-ami/pat-1, 98-arc/mar, 98-arc/nar, 98-igl/org, 98-nik/shi, 98-zie].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont.

Landolt-Börnstein New Series IV/8G

2.1.1 Alkanols, C1 - C4

19

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

190.00 200.00 210.00 220.00 230.00 240.00 250.00 260.00 270.00 280.00 290.00 293.15

ρ ± σ fit z kg ⋅ m−3

T K

879.47 ± 0.19 870.01 ± 0.16 860.83 ± 0.14 851.87 ± 0.12 843.10 ± 0.11 834.47 ± 0.10 825.95 ± 0.09 817.50 ± 0.08 809.07 ± 0.08 800.63 ± 0.08 792.14 ± 0.09 789.45 ± 0.09

298.15 300.00 310.00 320.00 330.00 340.00 350.00 360.00 370.00 380.00 390.00 400.00

1-Propanol

ρ ± σ fit z kg ⋅ m−3 785.15 ± 0.10 783.55 ± 0.10 774.84 ± 0.11 765.95 ± 0.13 756.85 ± 0.15 747.49 ± 0.18 737.85 ± 0.20 727.87 ± 0.24 717.53 ± 0.27 706.77 ± 0.31 695.56 ± 0.46 683.86 ± 0.61

[71-23-8]

T K

410.00 420.00 430.00 440.00 450.00 460.00 470.00 480.00 490.00 500.00 510.00

C3H8O

ρ ± σ fit z kg ⋅ m−3 670.34 ± 0.81 654.76 ± 1.03 638.22 ± 1.35 621.16 ± 1.59 603.43 ± 2.24 584.26 ± 2.72 562.34 ± 3.83 535.74 ± 4.03 501.66 ± 5.42 455.47 ± 8.47 383.00 ± 11.63

MW = 60.1

3

Tc = 536.70 K [89-tej/lee] ρc = 275.00 kg·m−3 [89-tej/lee] Table 1. Coefficients for the polynomial expansion equations. Standard deviations (see introduction): σ = 5.7712 · 10−1 (low temperature range), σc,w = (3.4844 · 10−1 combined temperature ranges, weighted), σc,uw = 2.0066 · 10−1 (combined temperature ranges, unweighted).

Coefficient

T = 150.00 to 410.00 K ρ = A + BT + CT 2 + DT 3 + …

1.01077 · 103 −3.99649 · 10−5 −6.64923 · 10−3 2.16751 · 10−5 −2.46167 · 10−8

A B C D E

T = 410.00 to 536.70 K ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)] [ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] 1.19032 −1.74429 · 10−2 1.13720 · 10−4 −2.75663 · 10−7

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 3 −3 − in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 273.15 819.28 ± 0.10 −0.08 51-kre(✕ ) 328.20 774.64 ± 1.50 −0.54 288.02 807.55 ± 0.10 −0.09 51-kre1) 330.62 772.55 ± 1.50 −0.58 298.12 799.50 ± 0.10 −0.15 51-kre1) 333.31 770.22 ± 1.50 −0.62 308.05 791.47 ± 0.10 −0.25 51-kre1) 335.56 768.25 ± 1.50 −0.66 318.18 783.12 ± 0.10 −0.38 51-kre(✕ ) 338.23 765.89 ± 1.50 −0.71 1)

Ref. (Symbol in Fig. 1) 51-kre1) 51-kre1) 51-kre1) 51-kre1) 51-kre1)

Not included in Fig. 1.

cont.

Landolt-Börnstein New Series IV/8G

20

2.1.1 Alkanols, C1 - C4

1-Propanol (cont.)

Table 2. (cont.) ρexp − ρcalc ρexp ± 2σ est T −3 kg ⋅ m−3 K kg ⋅ m 348.15 756.89 ± 1.50 −0.93 273.15 819.30 ± 0.50 −0.06 293.15 803.50 ± 0.50 −0.09 313.15 787.50 ± 0.50 −0.10 333.15 770.00 ± 0.50 −0.98 353.15 752.00 ± 0.50 −1.25 373.15 732.50 ± 0.50 −1.33 393.15 711.00 ± 0.60 −1.04 413.15 687.50 ± 0.60 0.38 433.15 660.00 ± 0.80 0.73 453.15 628.50 ± 1.00 −0.43 473.15 592.00 ± 1.00 −1.97 493.15 548.50 ± 1.00 −0.97 273.15 819.47 ± 0.10 0.11 293.15 803.50 ± 0.30 −0.09 414.80 687.50 ± 0.50 2.59 427.33 670.00 ± 0.50 2.39 439.00 653.30 ± 0.50 2.60 450.08 635.00 ± 0.50 1.19 459.44 620.40 ± 0.50 1.79 465.92 607.70 ± 0.50 0.31 474.16 592.30 ± 0.50 0.29 479.55 581.60 ± 0.50 0.51 498.27 537.60 ± 1.00 1.99 505.69 516.60 ± 2.00 3.60 513.26 499.20 ± 2.00 13.23 518.48 472.40 ± 3.00 8.21 523.37 449.90 ± 5.00 9.44 527.76 426.70 ± 5.00 11.75 529.84 412.70 ± 5.00 12.07 323.15 779.50 ± 0.20 0.10 333.15 771.30 ± 0.20 0.32 343.15 763.70 ± 0.20 1.41 153.15 917.00 ± 0.70 −2.12 163.15 908.00 ± 0.70 −2.46 173.15 899.60 ± 0.60 −2.21 183.15 890.80 ± 0.60 −2.38 193.15 882.50 ± 0.60 −2.12 203.15 874.50 ± 0.50 −1.64 213.15 866.80 ± 0.50 −0.96 223.15 858.70 ± 0.50 −0.77 1)

Ref. (Symbol in Fig. 1) 1)

51-kre 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 59-mck/ski(✕ ) 63-amb/tow1) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow1) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow1) 63-amb/tow1) 63-brz/har1) 63-brz/har1) 63-brz/har(✕ ) 67-kom/man1) 67-kom/man1) 67-kom/man1) 67-kom/man1) 67-kom/man1) 67-kom/man(✕ ) 67-kom/man1) 67-kom/man(✕ )

T K

233.15 243.15 253.15 263.15 273.15 283.15 293.15 298.15 303.15 293.15 298.15 303.15 320.00 340.00 360.00 380.00 400.00 420.00 440.00 460.00 470.00 483.83 303.15 313.15 298.15 308.15 318.15 333.15 298.15 288.15 293.15 298.15 303.15 308.15 303.15 150.00 150.00 170.00 170.00 190.00 190.00

ρexp ± 2σ est −3

kg ⋅ m

850.50 ± 0.40 842.70 ± 0.40 834.90 ± 0.40 826.80 ± 0.40 819.00 ± 0.30 811.10 ± 0.30 803.20 ± 0.30 799.50 ± 0.30 795.96 ± 0.04 803.61 ± 0.20 799.60 ± 0.20 795.61 ± 0.20 781.71 ± 0.20 764.40 ± 0.20 745.71 ± 0.20 725.26 ± 0.20 702.59 ± 0.20 677.31 ± 0.30 648.88 ± 0.30 616.11 ± 0.40 597.88 ± 0.50 571.43 ± 0.50 795.93 ± 0.10 787.62 ± 0.10 799.91 ± 0.15 791.85 ± 0.15 783.59 ± 0.15 770.80 ± 0.15 799.57 ± 0.02 807.40 ± 0.05 803.49 ± 0.05 799.35 ± 0.05 795.47 ± 0.05 791.41 ± 0.05 796.00 ± 0.05 922.70 ± 0.18 922.70 ± 0.18 903.50 ± 0.18 903.60 ± 0.18 886.50 ± 0.18 886.60 ± 0.18

ρexp − ρcalc Ref. (Symbol in Fig. 1) kg ⋅ m−3

−0.78 −0.49 −0.28 −0.45 −0.36 −0.38 −0.39 −0.13 0.31 0.02 −0.03 −0.04 −0.29 −0.66 −1.11 −1.41 −1.31 −0.53 −0.33 −1.56 −2.07 −0.40 0.28 0.02 0.28 0.21 0.07 −0.18 −0.06 −0.14 −0.10 −0.28 −0.18 −0.23 0.35 0.85 0.85 −1.03 −0.93 −0.81 −0.71

67-kom/man(✕ ) 67-kom/man(✕ ) 67-kom/man(✕ ) 67-kom/man1) 67-kom/man1) 67-kom/man1) 67-kom/man1) 67-kom/man1) 74-rao/nai-1(∆) 76-hal/ell1) 76-hal/ell1) 76-hal/ell1) 76-hal/ell1) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell1) 76-hal/ell1) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 78-red/nai-11) 78-red/nai-1(✕ ) 79-dia/tar1) 79-dia/tar1) 79-dia/tar1) 79-dia/tar(✕ ) 79-kiy/ben( ) 80-ben/kiy(◆) 80-ben/kiy(◆) 80-ben/kiy1) 80-ben/kiy(◆) 80-ben/kiy(◆) 81-nar/dha(∇) 82-zak(✕ ) 82-zak(✕ ) 82-zak(✕ ) 82-zak(✕ ) 82-zak(✕ ) 82-zak(✕ )

Not included in Fig. 1.

cont.

Landolt-Börnstein New Series IV/8G

2.1.1 Alkanols, C1 - C4 Table 2. (cont.) ρexp − ρcalc ρexp ± 2σ est T −3 kg ⋅ m−3 K kg ⋅ m 210.00 870.60 ± 0.17 0.21 210.00 870.10 ± 0.17 −0.29 230.00 854.40 ± 0.17 0.55 230.00 854.10 ± 0.17 0.25 250.00 838.50 ± 0.17 0.80 250.00 838.60 ± 0.17 0.90 270.00 823.00 ± 0.16 1.16 270.00 822.80 ± 0.16 0.96 290.00 807.20 ± 0.16 1.12 290.00 807.30 ± 0.16 1.22 310.00 791.40 ± 0.16 1.25 310.00 791.10 ± 0.16 0.95 330.00 774.30 ± 0.15 0.64 330.00 774.80 ± 0.15 1.14 1)

Ref. (Symbol in Fig. 1) 82-zak(✕ ) 82-zak(✕ ) 82-zak(✕ ) 82-zak(✕ ) 82-zak(✕ ) 82-zak(✕ ) 82-zak(✕ ) 82-zak(✕ ) 82-zak1) 82-zak1) 82-zak1) 82-zak1) 82-zak(✕ ) 82-zak(✕ )

T K

350.00 350.00 370.00 370.00 283.15 298.15 313.15 298.15 293.15 298.15 333.15 303.15 333.15

21

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m

kg ⋅ m−3

−3

757.60 ± 0.15 756.40 ± 0.15 739.60 ± 0.15 736.60 ± 0.15 811.45 ± 0.10 799.63 ± 0.10 787.46 ± 0.10 799.57 ± 0.03 803.78 ± 0.10 799.81 ± 0.10 770.58 ± 0.10 795.61 ± 0.10 770.64 ± 0.10

1.46 0.26 2.57 −0.43 −0.03 −0.00 −0.14 −0.06 0.19 0.18 −0.40 −0.04 −0.34

Ref. (Symbol in Fig. 1) 82-zak(✕ ) 82-zak(✕ ) 82-zak1) 82-zak(✕ ) 86-hei/sch(✕ ) 86-hei/sch1) 86-hei/sch(✕ ) 86-oga/mur( ) 86-wag/hei1) 86-wag/hei1) 86-wag/hei(✕ ) 87-pik1) 87-pik(✕ )

Not included in Fig. 1.

Further references: [1864-lan, 1871-ros, 1872-lin/von, 1879-bru, 1880-bru-3, 1881-nac/pag, 1882-sch-1, 1882-zan, 1883-sch-3, 1884-per, 1884-sch-6, 1884-zan, 1886-tra, 1889-ram/you, 1890-gar, 1891-jah, 1891-sch/kos, 1892-lan/jah, 1892-sch-1, 1893-eyk-1, 1894-sch, 1898-kah, 1898-lou, 1898-roh, 00-loo, 02-you/for, 05-dun, 08-dor/dvo, 08-ric/mat, 09-dor, 09-dor/roz, 09-hol/sag, 10-dor/pol, 10-dor/pol-1, 10-tim, 11-dor, 12-sch-2, 12-wre, 13-atk/wal, 13-bri-1, 14-eng/tur, 14-kre/mei, 14-low, 16-wro/rei, 17-jae, 18-her-2, 19-eyk, 21-bru/cre, 21-rei/hic, 23-bru, 23-tim, 23-wil/smi, 24-par/sch, 25-nor/ash, 25-pal/con, 25-per, 26-han, 26-mun, 26-par/huf, 26-sch, 27-mou/duf, 28-llo/bro, 29-ber, 30-bil/fis-1, 33-azi/bha, 33-but/tho, 33-kil, 33-tre/wat, 33-vos/con, 34-tim/del, 35-bra/fel, 35-cou/hop, 35-hen, 36-spe, 36-tom, 39-lar/hun, 42-mul, 42-was/bro, 45-add, 48-vog-2, 48-wei, 49-hat, 49-tsc/ric, 49-tsv/mar, 50-jac, 50-mum/phi, 50-pic/zie, 50-sac/sau, 50-tei/gor, 51-dim/lan, 51-tei/gor, 52-coo, 53-ani, 53-ani-1, 53-mcc/jon, 54-pur/bow, 55-bak, 57-mal/mal, 57-rom, 58-lin/van, 58-mur/van, 59-ale, 60-cop/fin, 61-ogi/cor, 62-bro/smi, 62-chu/tho, 62-par/mis, 63-gol/bag, 63-hov/sea, 63-mcc/lai, 63-mik/kim, 63-pra/van, 64-ska/kay, 65-fin/kid, 66-gur/raj, 66-kil/che, 67-gol/per, 68-ano, 68-joh, 68-pfl/pop, 69-bro/foc, 69-fin/cop, 69-smi/kur, 70-gur/raj, 70-kri/kom, 70-str/svo, 72-nie/nov, 72-udo/maz, 73-daw/new, 73-svo/ves, 74-dut/mat, 74-rao/nai, 75-mat/fer, 75-tok, 76-for/ben, 76-kat/nit, 76-kow/kas, 76-nag/oht, 76-red/nai, 76-wes-1, 77-hwa/rob, 77-tre/ben, 78-dap/don, 79-cha/ses-1, 79-ern/gli, 79-jim/paz, 80-arc/bla, 80-fuk/ogi, 80-yos/tak, 81-kum/pra, 81-nai/nai, 81-sjo/dyh, 81-tas/ara, 81-won/chu, 82-diz/mar, 82-kar/red, 82-nai/nai, 82-ort, 82-ven/dha, 83-fuk/ogi, 83-pik-1, 83-pik-2, 83-rau/ste, 83-tri, 84-sak/nak, 85-fer/ber, 85-fer/pin, 85-mat/ben, 85-mat/ben-1, 85-nag-2, 85-ort/paz-1, 85-ped/dav, 85-zhu/dur, 86-ash/sri, 86-ber/wec-1, 86-lep/mat, 86-mah/daw, 86-miy/hay, 86-san/sha, 86-tan/toy, 87-ber-2, 87-ber-3, 87-kub/tan, 87-oga/mur, 87-rat/sin-3, 88-jad/fra, 88-nag-2, 88-ort/mat, 89-ala/sal, 89-nao/sur, 89-ort/sus, 89-pae/con, 89-sus/ort, 90-cha/kat, 90-sri/nai, 91-cab/bel, 91-gar/her, 91-kat/tan, 91-ram/muk, 92-kum/sre, 93-ami/ara, 94-hia/tak, 94-hia/tak-1, 94-kim/lee, 94-pap/pan, 94-pap/pan-1, 94-rom/pel, 94-sin/kal, 94-ven/ven, 95-hia/tak, 95-hia/tak-1, 95-red/ram-1, 96-elb, 96-nik/jad, 96-nik/mah, 97-com/fra, 98-ami/ban, 98-ami/pat-1, 98-nik/shi, 98-pal/sha].

cont.

Landolt-Börnstein New Series IV/8G

22

2.1.1 Alkanols, C1 - C4

ρ

ρ

1-Propanol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

150.00 160.00 170.00 180.00 190.00 200.00 210.00 220.00 230.00 240.00 250.00 260.00 270.00 280.00

ρ ± σ fit kg ⋅ m−3 921.85 ± 0.27 913.19 ± 0.26 904.53 ± 0.25 895.89 ± 0.24 887.31 ± 0.23 878.81 ± 0.22 870.39 ± 0.21 862.07 ± 0.21 853.85 ± 0.20 845.73 ± 0.19 837.70 ± 0.18 829.74 ± 0.18 821.84 ± 0.17 813.96 ± 0.16

T K

290.00 293.15 298.15 300.00 310.00 320.00 330.00 340.00 350.00 360.00 370.00 380.00 390.00 400.00

ρ ± σ fit kg ⋅ m−3 806.08 ± 0.15 803.59 ± 0.15 799.63 ± 0.15 798.16 ± 0.15 790.15 ± 0.14 782.00 ± 0.13 773.66 ± 0.13 765.06 ± 0.12 756.14 ± 0.12 746.82 ± 0.12 737.03 ± 0.13 726.67 ± 0.14 715.66 ± 0.18 703.90 ± 0.22

T K

410.00 420.00 430.00 440.00 450.00 460.00 470.00 480.00 490.00 500.00 510.00 520.00 530.00

ρ ± σ fit kg ⋅ m−3 691.28 ± 0.29 677.84 ± 0.54 663.81 ± 0.53 649.21 ± 0.53 633.93 ± 0.55 617.67 ± 0.58 599.95 ± 0.63 580.14 ± 0.71 557.41 ± 0.84 530.62 ± 1.06 498.18 ± 1.49 457.21 ± 2.58 399.44 ± 8.86

Landolt-Börnstein New Series IV/8G

2.1.1 Alkanols, C1 - C4 2- Propanol

[67-63-0]

23 C3H8O

MW = 60.1

4

Tc = 508.00 K [89-tej/lee] ρc = 273.00 kg·m−3 [89-tej/lee] Table 1. Coefficients for the polynomial expansion equations. Standard deviations (see introduction): σ = 9.7228 · 10−1 (low temperature range), σc,w = (9.9994 · 10−1 combined temperature ranges, weighted), σc,uw = 5.4125 · 10−1 (combined temperature ranges, unweighted).

Coefficient

T = 213.15 to 400.00 K ρ = A + BT + CT 2 + DT 3 + …

9.93868 · 102 −3.40464 · 10−5 −6.95191 · 10−3 2.40158 · 10−5 −2.92637 · 10−8

A B C D E

T = 400.00 to 508.00 K ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)] [ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] 1.42642 −2.55851 · 10−2 2.00711 · 10−4 −5.71341 · 10−7

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 1) 303.15 778.60 ± 0.45 1.70 33-azi/bha 443.72 595.70 ± 0.50 −1.33 313.15 769.80 ± 0.45 1.59 33-azi/bha1) 450.70 581.50 ± 0.50 −2.04 323.15 761.70 ± 0.45 2.50 33-azi/bha1) 458.45 564.00 ± 0.50 −3.06 333.15 750.90 ± 0.45 1.11 33-azi/bha(✕ ) 465.13 548.00 ± 0.50 −3.12 297.97 781.04 ± 0.10 −0.25 469.84 535.70 ± 0.50 −2.93 45-kol/bur(∆) 298.15 781.48 ± 0.10 0.34 54-tha/row(∇) 474.89 522.20 ± 1.00 −1.60 293.15 785.50 ± 0.20 0.17 56-tor-11) 480.40 505.50 ± 1.00 −0.06 313.15 768.40 ± 0.20 0.19 56-tor-1(✕ ) 486.34 485.20 ± 1.00 2.37 333.15 749.70 ± 0.20 −0.09 56-tor-1(✕ ) 491.20 465.80 ± 1.00 4.68 213.15 849.10 ± 0.50 −1.08 58-cos/bow(✕ ) 495.79 441.80 ± 1.00 4.75 233.15 834.10 ± 0.50 0.24 58-cos/bow(✕ ) 500.43 416.50 ± 1.00 9.31 253.15 818.30 ± 0.50 0.53 58-cos/bow(✕ ) 504.22 384.90 ± 1.00 10.32 273.15 802.70 ± 0.50 0.99 58-cos/bow(✕ ) 506.68 349.30 ± 1.00 7.80 293.15 786.20 ± 0.40 0.87 58-cos/bow1) 300.00 779.00 ± 1.00 −0.58 313.15 768.80 ± 0.40 0.59 58-cos/bow1) 320.00 763.00 ± 1.00 0.92 333.15 750.20 ± 0.50 0.41 58-cos/bow1) 340.00 745.00 ± 1.00 1.93 353.15 730.30 ± 0.50 0.88 58-cos/bow(✕ ) 360.00 724.00 ± 1.00 2.15 373.15 708.00 ± 0.60 1.69 58-cos/bow(✕ ) 380.00 702.00 ± 1.00 4.39 393.15 683.00 ± 0.60 3.43 58-cos/bow(✕ ) 400.00 676.00 ± 1.50 6.59 413.15 656.50 ± 0.60 7.69 58-cos/bow(✕ ) 420.00 648.00 ± 1.50 10.24 433.15 626.40 ± 0.60 10.54 58-cos/bow(✕ ) 440.00 619.00 ± 1.50 15.16 293.15 785.11 ± 0.10 −0.22 59-bar/dod( ) 460.00 585.00 ± 1.50 21.47 407.35 660.50 ± 0.50 2.49 63-amb/tow(✕ ) 480.00 541.00 ± 2.00 34.03 422.33 635.30 ± 0.50 1.34 63-amb/tow(✕ ) 500.00 470.00 ± 2.00 59.70

1)

Ref. (Symbol in Fig. 1) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah(✕ ) 64-dan/bah(✕ ) 64-dan/bah1) 64-dan/bah1)

Not included in Fig. 1.

cont.

Landolt-Börnstein New Series IV/8G

24

2.1.1 Alkanols, C1 - C4

2- Propanol (cont.)

Table 2. (cont.) ρexp − ρcalc ρexp ± 2σ est T −3 kg ⋅ m−3 K kg ⋅ m 436.38 610.40 ± 0.50 0.14 298.15 780.93 ± 0.20 −0.21 303.15 776.75 ± 0.20 −0.15 320.00 761.72 ± 0.20 −0.36 340.00 742.37 ± 0.20 −0.70 360.00 720.76 ± 0.20 −1.09 380.00 696.49 ± 0.20 −1.12 400.00 669.17 ± 0.20 −0.24 420.00 638.28 ± 0.20 0.52 430.00 621.15 ± 0.25 −0.07 213.15 847.60 ± 0.50 −2.58 233.15 834.00 ± 0.50 0.14 253.15 817.40 ± 0.50 −0.37 273.15 801.30 ± 0.50 −0.41 275.00 798.80 ± 0.40 −1.41 300.00 779.55 ± 0.40 −0.03 325.00 757.02 ± 0.40 −0.47 350.00 731.84 ± 0.40 −0.95 375.00 702.89 ± 0.40 −1.11 400.00 669.36 ± 0.40 −0.05 425.00 630.00 ± 1.00 0.43 450.00 581.99 ± 2.00 −2.96 475.00 519.76 ± 2.00 −3.70 500.00 425.22 ± 5.00 14.92 508.30 273.17 ± 0.00 5.23 1)

Ref. (Symbol in Fig. 1) 63-amb/tow(✕ ) 76-hal/ell1) 76-hal/ell1) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-kat/nit(✕ ) 76-kat/nit(✕ ) 76-kat/nit(✕ ) 76-kat/nit(✕ ) 78-amb/cou-1(✕ ) 78-amb/cou-11) 78-amb/cou-1(✕ ) 78-amb/cou-1(✕ ) 78-amb/cou-1(✕ ) 78-amb/cou-1(✕ ) 78-amb/cou-1(✕ ) 78-amb/cou-1(✕ ) 78-amb/cou-1(✕ ) 78-amb/cou-11) 78-amb/cou-11)

T K

313.15 303.15 298.15 298.15 298.15 303.15 308.15 313.15 318.15 323.15 303.15 333.15 278.15 288.15 298.15 308.15 318.15 293.15 298.15 303.15 313.15 323.15 298.15 303.15 308.15

ρexp ± 2σ est

ρexp − ρcalc

−3

kg ⋅ m

Ref. (Symbol in Fig. 1)

768.98 ± 0.20 776.56 ± 0.15 781.02 ± 0.15 781.01 ± 0.15 781.70 ± 0.30 777.60 ± 0.30 773.50 ± 0.30 769.30 ± 0.30 765.20 ± 0.30 761.30 ± 0.30 776.59 ± 0.40 749.33 ± 0.40 797.26 ± 0.30 798.13 ± 0.30 780.80 ± 0.30 772.20 ± 0.30 763.29 ± 0.30 785.10 ± 0.30 780.90 ± 0.30 776.70 ± 0.30 767.80 ± 0.30 759.10 ± 0.20 781.23 ± 0.20 776.95 ± 0.20 773.46 ± 0.20

0.77 −0.34 −0.12 −0.13 0.56 0.70 0.91 1.09 1.45 2.10 −0.31 −0.46 −0.40 8.65 −0.34 −0.39 −0.46 −0.23 −0.24 −0.20 −0.41 −0.10 0.09 0.05 0.87

66-kat/shi(✕ ) 83-pik-2(◆) 83-wec/byl( ) 83-wec/byl( ) 87-isl/qua1) 87-isl/qua1) 87-isl/qua1) 87-isl/qua1) 87-isl/qua(✕ ) 87-isl/qua(✕ ) 87-pik1) 87-pik(✕ ) 88-sak(✕ ) 88-sak1) 88-sak1) 88-sak1) 88-sak(✕ ) 89-pae/con1) 89-pae/con1) 89-pae/con1) 89-pae/con1) 89-pae/con(✕ ) 98-nik/shi(✕ ) 98-nik/shi(✕ ) 98-nik/shi(✕ )

kg ⋅ m

−3

Not included in Fig. 1.

Further references: [1880-bru-1, 1883-sch-3, 21-bru/cre, 21-leb, 23-bru, 25-nor/ash, 25-par/kel, 26-mat, 26-mun, 28-par/kel, 29-kel, 35-but/ram, 38-ols/was, 39-lar/hun, 39-par/moo, 44-ira, 46-kre/now, 50-par/gol, 52-cap/mug, 53-ani-1, 53-par/cha, 56-goe/mcc, 58-ano-5, 58-mur/van, 59-bur/can, 61-ogi/cor, 62-chu/tho, 63-pra/van-1, 65-fin/kid, 66-kat/pra-1, 67-fre, 67-gol/per, 68-ano, 68-ver, 69-kom/kri, 69-ver/lau, 70-ver, 71-nag/oht, 73-nag/oht, 74-pur/pol, 75-tok, 76-nag/oht, 76-sri/kul, 80-edu/boy, 80-kas/izy, 80-yos/tak, 82-kar/red, 82-ven/dha, 83-fuk/ogi, 83-tri, 83-wec, 84-ped/sal, 85-dri/ras, 85-mat/ben, 85-mat/ben-1, 85-nag-1, 85-rao/red, 86-ber/wec, 86-hne/cib, 86-mou/nai, 87-ber-1, 87-ber-4, 88-nag-1, 89-kat/tan, 89-nao/sur, 91-ace/ped-1, 91-kat/tan, 92-ard/say-1, 92-kum/sre, 94-hia/tak, 94-sin/kal, 95-hia/tak, 96-nik/jad, 96-nik/mah].

cont.

Landolt-Börnstein New Series IV/8G

25

ρ

ρ

2.1.1 Alkanols, C1 - C4

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

210.00 220.00 230.00 240.00 250.00 260.00 270.00 280.00 290.00 293.15 298.15

Landolt-Börnstein New Series IV/8G

ρ ± σ fit kg ⋅ m−3 852.78 ± 0.63 844.56 ± 0.56 836.41 ± 0.50 828.33 ± 0.44 820.30 ± 0.40 812.28 ± 0.36 804.25 ± 0.33 796.15 ± 0.30 787.95 ± 0.28 785.33 ± 0.27 781.14 ± 0.27

T K

300.00 310.00 320.00 330.00 340.00 350.00 360.00 370.00 380.00 390.00 400.00

ρ ± σ fit kg ⋅ m−3 779.58 ± 0.26 770.98 ± 0.26 762.08 ± 0.26 752.80 ± 0.26 743.07 ± 0.28 732.79 ± 0.29 721.85 ± 0.31 710.16 ± 0.34 697.61 ± 0.37 684.06 ± 0.42 669.41 ± 0.48

T K

410.00 420.00 430.00 440.00 450.00 460.00 470.00 480.00 490.00 500.00

ρ ± σ fit kg ⋅ m−3 653.83 ± 0.63 637.76 ± 0.65 621.22 ± 0.68 603.84 ± 0.71 584.95 ± 0.75 563.53 ± 0.81 538.18 ± 0.89 506.97 ± 1.00 466.79 ± 1.15 410.30 ± 1.39

26

2.1.1 Alkanols, C1 - C4

1-Butanol

[71-36-3]

C4H10O

MW = 74.12

5

Tc = 562.40 K [89-tej/lee] ρc = 270.00 kg·m−3 [89-tej/lee]

Table 1. Coefficients for the polynomial expansion equations. Standard deviations (see introduction): σ = 3.7574 · 10−1 (low temperature range), σc,w = (5.9442 · 10−1 combined temperature ranges, weighted), σc,uw = 4.3091 · 10−1 (combined temperature ranges, unweighted).

Coefficient

T = 192.35 to 420.00 K ρ = A + BT + CT 2 + DT 3 + …

1.15309 · 103 −2.13475 5.15573 · 10−3 −6.38112 · 10−6

A B C D

T = 420.00 to 562.40 K ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)] [ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] 1.16613 −1.80981 · 10−2 1.25770 · 10−4 −3.17257 · 10−7

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m crystal 197.57 882.41 ± 0.30 −0.95 78.15 1030.0 ± 5.0 30-bilfis-1 204.09 877.29 ± 0.30 −0.62 liquid 217.71 866.76 ± 0.30 −0.09 273.15 824.70 ± 0.20 0.09 28-tim/mar(✕ ) 217.82 866.54 ± 0.30 −0.23 288.15 813.35 ± 0.20 −0.02 28-tim/mar1) 227.45 859.32 ± 0.30 0.14 303.15 802.04 ± 0.20 0.07 28-tim/mar1) 233.70 854.48 ± 0.20 0.15 193.15 887.20 ± 0.50 0.08 29-smy/sto(✕ ) 234.79 853.49 ± 0.20 −0.00 203.15 879.30 ± 0.50 0.61 29-smy/sto(✕ ) 235.45 853.05 ± 0.20 0.06 213.15 871.30 ± 0.50 0.79 29-smy/sto(✕ ) 240.28 849.36 ± 0.20 0.07 223.15 863.40 ± 0.50 0.85 29-smy/sto1) 249.85 841.97 ± 0.20 −0.07 233.15 855.60 ± 0.50 0.84 29-smy/sto1) 255.01 838.52 ± 0.20 0.36 243.15 847.90 ± 0.50 0.79 29-smy/sto1) 261.87 832.64 ± 0.20 −0.39 253.15 840.20 ± 0.40 0.64 29-smy/sto(✕ ) 273.15 823.80 ± 0.20 −0.81 263.15 832.80 ± 0.40 0.73 29-smy/sto(✕ ) 273.15 824.29 ± 0.20 −0.32 273.15 825.00 ± 0.40 0.39 29-smy/sto1) 298.15 805.61 ± 0.20 −0.19 283.15 817.30 ± 0.40 0.17 29-smy/sto1) 273.15 824.60 ± 0.20 −0.01 293.15 809.80 ± 0.40 0.20 29-smy/sto1) 298.15 805.70 ± 0.20 −0.10 303.15 802.20 ± 0.40 0.23 29-smy/sto1) 463.15 625.10 ± 0.60 −8.32 313.15 794.50 ± 0.40 0.28 29-smy/sto1) 473.15 601.90 ± 0.60 −16.39 323.15 786.70 ± 0.40 0.40 29-smy/sto1) 483.15 595.60 ± 0.60 −6.95 333.15 778.70 ± 0.40 0.52 29-smy/sto1) 493.15 575.90 ± 0.60 −9.92 343.15 770.30 ± 0.50 0.49 29-smy/sto1) 503.15 561.80 ± 0.60 −5.68 353.15 761.60 ± 0.50 0.45 29-smy/sto1) 513.15 542.20 ± 0.70 −4.54 363.15 752.70 ± 0.50 0.52 29-smy/sto(✕ ) 523.15 519.70 ± 0.70 −2.83 192.35 886.07 ± 0.30 −1.74 31-ton/ueh(✕ ) 533.15 491.70 ± 0.70 −1.65 1)

Ref. (Symbol in Fig. 1) 31-ton/ueh(✕ ) 31-ton/ueh(✕ ) 31-ton/ueh(✕ ) 31-ton/ueh(✕ ) 31-ton/ueh(✕ ) 31-ton/ueh(✕ ) 31-ton/ueh(✕ ) 31-ton/ueh(✕ ) 31-ton/ueh(✕ ) 31-ton/ueh(✕ ) 31-ton/ueh(✕ ) 31-ton/ueh(✕ ) 31-ton/ueh(✕ ) 32-ell/rei(✕ ) 32-ell/rei1) 39-jon/chr(✕ ) 39-jon/chr1) 55-kay/don(✕ ) 55-kay/don(✕ ) 55-kay/don(✕ ) 55-kay/don(✕ ) 55-kay/don(✕ ) 55-kay/don(✕ ) 55-kay/don(✕ ) 55-kay/don(✕ )

Not included in Fig. 1.

cont.

Landolt-Börnstein New Series IV/8G

2.1.1 Alkanols, C1 - C4 Table 2. (cont.) ρexp − ρcalc ρexp ± 2σ est T −3 kg ⋅ m−3 K kg ⋅ m 543.15 458.50 ± 0.80 1.70 553.15 414.60 ± 0.90 7.50 562.89 267.00 ± 0.00 ?.00 293.15 809.90 ± 0.30 0.30 298.15 806.10 ± 0.30 0.30 303.15 802.20 ± 0.30 0.23 313.15 794.50 ± 0.30 0.28 323.15 786.80 ± 0.30 0.50 333.15 778.90 ± 0.30 0.72 343.15 770.70 ± 0.40 0.89 353.15 762.20 ± 0.40 1.05 213.15 867.70 ± 0.50 −2.81 233.15 852.80 ± 0.50 −1.96 253.15 838.20 ± 0.50 −1.36 273.15 823.40 ± 0.50 −1.21 293.15 808.60 ± 0.40 −1.00 313.15 793.60 ± 0.40 −0.62 333.15 779.00 ± 0.50 0.82 353.15 761.60 ± 0.50 0.45 373.15 743.40 ± 0.50 0.55 393.15 723.70 ± 0.50 0.75 413.15 701.60 ± 0.60 0.45 433.15 678.70 ± 0.60 2.26 443.15 654.50 ± 0.60 −8.07 303.15 802.00 ± 0.30 0.03 328.15 782.90 ± 0.30 0.63 348.15 767.00 ± 0.40 1.48 368.15 748.20 ± 0.40 0.64 273.15 824.59 ± 0.10 -0.02 293.15 809.60 ± 0.30 0.00 440.08 669.40 ± 0.50 2.50 451.72 653.80 ± 0.50 3.54 462.05 640.10 ± 0.50 5.04 469.47 627.90 ± 0.50 3.99 475.77 618.20 ± 0.50 3.96 481.90 608.70 ± 1.00 4.13 489.78 595.00 ± 1.00 3.40 499.72 576.40 ± 1.00 2.40 508.23 559.20 ± 1.00 1.89 515.59 543.70 ± 1.00 2.50 521.20 531.40 ± 1.00 3.81 530.10 508.00 ± 1.00 5.10 534.05 489.60 ± 1.00 −0.82 1)

Ref. (Symbol in Fig. 1) 55-kay/don(✕ ) 55-kay/don(✕ ) 55-kay/don1) 55-kus1) 55-kus1) 55-kus1) 55-kus1) 55-kus1) 55-kus1) 55-kus1) 55-kus(✕ ) 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow1) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-lin/van1) 58-lin/van1) 58-lin/van(✕ ) 58-lin/van(✕ ) 59-mck/ski(✕ ) 63-amb/tow1) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ )

T K

548.85 200.00 220.00 240.00 260.00 280.00 300.00 320.00 340.00 360.00 380.00 400.00 420.00 440.00 460.00 480.00 500.00 520.00 540.00 560.00 513.15 518.15 523.15 528.15 533.15 538.15 543.15 548.15 553.15 558.15 273.15 293.15 313.15 333.15 353.15 373.15 393.15 413.15 433.15 453.15 473.15 493.15 513.15

27

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m

kg ⋅ m−3

−3

436.50 ± 1.00 876.00 ± 1.50 865.00 ± 1.50 846.00 ± 1.50 832.00 ± 1.50 817.00 ± 1.50 803.00 ± 1.50 787.00 ± 1.50 770.00 ± 1.50 752.00 ± 1.50 732.00 ± 1.50 711.00 ± 2.00 690.00 ± 2.00 663.00 ± 2.00 637.00 ± 2.00 610.00 ± 2.00 577.00 ± 2.00 540.00 ± 2.00 485.00 ± 2.50 380.00 ± 6.00 548.30 ± 3.00 537.70 ± 3.00 526.20 ± 3.00 514.20 ± 3.00 501.30 ± 3.00 486.80 ± 3.00 470.00 ± 3.00 450.00 ± 3.00 426.10 ± 3.00 391.60 ± 3.00 826.00 ± 0.50 810.00 ± 0.50 795.00 ± 0.50 779.00 ± 1.00 762.00 ± 1.00 743.00 ± 1.00 723.00 ± 1.00 702.00 ± 1.00 676.00 ± 1.50 697.00 ± 1.50 617.00 ± 1.50 582.00 ± 2.00 541.00 ± 2.00

5.68 −5.32 −0.03 −3.51 −2.43 −2.49 −1.39 −1.82 −2.47 −3.04 −4.23 −4.71 −3.20 −4.01 −1.11 2.40 3.52 9.39 15.67 29.03 1.56 2.55 3.67 5.52 7.95 10.58 13.20 15.71 19.00 21.09 1.39 0.40 0.78 0.82 0.85 0.15 0.05 0.85 -0.44 48.82 −1.29 −3.82 −5.74

Ref. (Symbol in Fig. 1) 63-amb/tow(✕ ) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah(✕ ) 64-dan/bah(✕ ) 64-dan/bah1) 64-ska/kay1) 64-ska/kay1) 64-ska/kay1) 64-ska/kay1) 64-ska/kay1) 64-ska/kay1) 64-ska/kay1) 64-ska/kay(✕ ) 64-ska/kay(✕ ) 64-ska/kay(✕ ) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1)

Not included in Fig. 1.

cont.

Landolt-Börnstein New Series IV/8G

28

2.1.1 Alkanols, C1 - C4

1-Butanol (cont.) Table 2. (cont.) ρexp − ρcalc ρexp ± 2σ est T −3 kg ⋅ m−3 K kg ⋅ m 533.15 490.00 ± 2.00 −3.35 543.15 457.00 ± 2.00 0.20 553.15 408.00 ± 3.00 0.90 559.15 343.00 ± 3.00 −17.71 560.15 314.00 ± 5.00 −35.06 186.15 891.20 ± 0.70 −2.00 193.15 885.40 ± 0.70 −1.72 203.15 877.50 ± 0.60 −1.19 213.15 869.60 ± 0.60 −0.91 223.15 862.20 ± 0.50 −0.35 233.15 854.70 ± 0.50 −0.06 243.15 847.10 ± 0.50 −0.01 253.15 839.50 ± 0.40 −0.06 263.15 831.80 ± 0.40 −0.27 273.15 824.30 ± 0.40 −0.31 283.15 816.60 ± 0.30 −0.53 293.15 809.10 ± 0.30 −0.50 298.15 805.40 ± 0.30 −0.40 303.15 801.95 ± 0.04 −0.02 293.15 809.56 ± 0.20 −0.04 298.15 805.75 ± 0.20 −0.05 303.15 801.91 ± 0.20 −0.06 320.00 788.73 ± 0.20 −0.09 340.00 772.32 ± 0.20 −0.15 360.00 754.76 ± 0.20 −0.28 380.00 735.73 ± 0.20 −0.50 1)

Ref. (Symbol in Fig. 1) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr1) 67-kom/man1) 67-kom/man1) 67-kom/man1) 67-kom/man1) 67-kom/man1) 67-kom/man1) 67-kom/man1) 67-kom/man(✕ ) 67-kom/man(✕ ) 67-kom/man1) 67-kom/man1) 67-kom/man1) 67-kom/man1) 74-rao/nai-1(∆) 76-hal/ell1) 76-hal/ell1) 76-hal/ell1) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ )

T K

400.00 420.00 440.00 460.00 470.00 480.00 490.00 213.15 233.15 253.15 273.15 303.15 313.15 298.15 308.15 318.15 333.15 298.15 303.15 283.15 298.15 313.15 298.15 298.15 303.15 333.15

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

714.96 ± 0.20 692.25 ± 0.20 667.32 ± 0.20 639.77 ± 0.25 624.85 ± 0.25 608.98 ± 0.30 592.03 ± 0.30 869.20 ± 0.50 853.90 ± 0.50 839.00 ± 0.50 824.30 ± 0.50 802.09 ± 0.10 794.51 ± 0.10 805.84 ± 0.15 798.02 ± 0.15 790.18 ± 0.15 778.10 ± 0.15 805.83 ± 0.02 802.01 ± 0.05 817.02 ± 0.10 805.76 ± 0.10 794.22 ± 0.10 805.74 ± 0.02 805.74 ± 0.05 801.91 ± 0.15 778.22 ± 0.15

−0.75 −0.95 0.31 1.66 1.75 1.38 0.80 −1.31 −0.86 −0.56 −0.31 0.12 0.29 0.04 −0.10 −0.11 −0.08 0.03 0.04 −0.11 −0.04 −0.00 −0.06 −0.06 −0.06 0.04

kg ⋅ m

Ref. (Symbol in Fig. 1) 76-hal/ell(✕ ) 76-hal/ell1) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-kat/nit(✕ ) 76-kat/nit1) 76-kat/nit1) 76-kat/nit1) 78-red/nai-11) 78-red/nai-1(✕ ) 79-dia/tar1) 79-dia/tar1) 79-dia/tar(✕ ) 79-dia/tar(✕ ) 79-kiy/ben( ) 81-nar/dha(◆) 86-hei/sch(✕ ) 86-hei/sch1) 86-hei/sch(✕ ) 86-oga/mur( ) 87-oga/mur(∇) 87-pik1) 87-pik(✕ )

Not included in Fig. 1.

Further references: [1864-lan, 1871-lie/ros, 1880-bru-1, 1881-pri/han, 1883-sch-3, 1884-zan, 1886-tra, 1893-eyk-1, 1898-kah, 00-loo, 06-car/fer, 08-dor/dvo, 08-ric/mat, 13-atk/wal, 14-low, 15-pea, 19-eyk, 19-ort/jon, 19-rei/ral, 21-bru/cre, 21-rei/hic, 22-her/sch, 23-pop, 23-wil/smi, 24-ter, 25-nor/ash, 25-pal/con, 25-per, 26-mat, 26-mun, 27-cla/rob, 27-ver/coo, 28-llo/bro, 29-ber, 29-jon, 29-mah/das, 29-pre, 30-bil/fis-1, 31-smy/wal, 31-sto/hul, 32-ern/lit, 33-azi/bha, 33-but/tho, 33-nev/jat, 33-tre/wat, 33-vos/con, 35-bra/fel, 35-bru/fur, 35-but/ram, 35-hen, 35-kef/mcl, 36-tom, 39-all/lin, 39-lar/hun, 41-hus/age, 42-mul, 42-sny/gil, 43-bru/bog, 44-was/str, 45-add, 46-kre/now, 48-con/elv, 48-jon/bow, 48-laz, 48-vog-2, 48-wei, 49-tsc/ric, 49-tsv/mar, 50-mum/phi, 50-pic/zie, 50-sac/sau, 51-sew, 51-tei/gor, 52-coo, 52-dun/was, 52-von, 53-ani, 53-mcc/jon, 53-par/cha, 54-jon/mcc, 54-pur/bow, 54-skr/mur, 55-bou/cle, 55-dan/col, 55-sin/she, 56-rus/ame, 56-tor-1, 57-mur/las, 57-rao/rao, 57-rom, 58-ano-5, 58-hol/len, 58-lin/tua, 59-ale, 59-ell/raz, 60-cop/fin, 60-tje, 61-bel/shu-1, 62-bro/smi, 62-par/mis, 63-gol/bag, 63-hov/sea, 63-man/she, 63-man/she-1, 63-mcc/lai, 63-sub/rao-1, 64-sta/kor, 65-fin/kid, 65-vij/des, 66-vij/des, 67-dei, 67-gol/per, 67-mur/rao, 67-vij/des-1, 68-ano, 69-fin/cop, 69-smi/kur, 69-sub/nag, 70-gal, 70-kat/kon, 70-kri/kom-1, 71-kat/lob, 72-bon/pik, 73-dak/rao, 73-dak/vee, 73-daw/new, 73-khi/ale, 73-svo/ves, 74-dut/mat, 74-rao/nai, 75-kub/tan, 75-mat/fer] cont.

Landolt-Börnstein New Series IV/8G

2.1.1 Alkanols, C1 - C4

29

ρ

ρ

[76-bul/pro, 76-kow/kas, 76-red/nai, 77-rat/sal, 77-tre/ben, 78-dap/don, 78-sac/pes, 79-cha/ses-1, 79-jim/paz, 79-kum/pra, 79-sah/hay, 80-arc/bla, 80-fuk/ogi, 80-sue/mul, 81-nai/nai, 81-sjo/dyh, 82-ber/rog-1, 82-kar/red, 82-nai/nai, 82-ort, 82-ven/dha, 83-fuk/ogi, 83-pik-1, 83-pik-2, 83-rau/ste, 83-tri, 84-ber/pen, 84-sak/nak, 85-fer/pin, 85-mat/ben, 85-mat/ben-1, 85-ort/paz-1, 85-sar/paz, 86-ash/sri, 86-gat/woo, 86-gou/tom, 86-lep/mat, 86-mah/daw, 86-miy/hay, 86-san/sha, 86-tan/toy, 87-ber-5, 87-ber-7, 87-fer/ber, 87-kri/cho, 87-kub/tan, 87-nag, 87-ogi/ara, 88-fer/lap, 88-nag-2, 89-ala/sal, 89-mac/fra, 89-nao/sur, 89-ort/sus, 89-vij/nai, 90-cha/kat, 90-sri/nai, 90-vij/nai, 91-cab/bel, 91-fen/wan, 91-gar/her, 91-ram/muk, 92-ban/san, 92-gra/san, 92-tan/mur, 93-ami/ara, 93-ami/rai, 93-sus/ort, 94-kim/lee, 94-pap/pan-1, 94-yu /tsa-1, 95-fra/jim, 95-fra/men, 95-red/ram-1, 96-bha/mak, 96-dej/gon-1, 96-dom/rod, 96-elb, 96-gon/ort, 96-nik/jad, 96-nik/mah, 98-ami/ban, 98-ami/pat-1, 98-nik/shi].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont.

Landolt-Börnstein New Series IV/8G

30

2.1.1 Alkanols, C1 - C4

1-Butanol (cont.) Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

190.00 200.00 210.00 220.00 230.00 240.00 250.00 260.00 270.00 280.00 290.00 293.15 298.15 300.00

ρ ± σ fit kg ⋅ m−3 889.84 ± 0.48 881.32 ± 0.42 873.06 ± 0.37 865.03 ± 0.32 857.19 ± 0.29 849.51 ± 0.25 841.93 ± 0.23 834.43 ± 0.21 826.96 ± 0.19 819.49 ± 0.17 811.98 ± 0.17 809.60 ± 0.17 805.80 ± 0.17 804.39 ± 0.17

d-2-Butanol

ρ ± σ fit kg ⋅ m−3

T K

T K

796.68 ± 0.17 788.82 ± 0.18 780.76 ± 0.20 772.47 ± 0.22 763.91 ± 0.24 755.04 ± 0.27 745.83 ± 0.31 736.23 ± 0.35 726.20 ± 0.40 715.71 ± 0.46 704.73 ± 0.53 693.20 ± 0.62 680.65 ± 0.70 667.01 ± 0.71

310.00 320.00 330.00 340.00 350.00 360.00 370.00 380.00 390.00 400.00 410.00 420.00 430.00 440.00

[4221-99-2]

450.00 460.00 470.00 480.00 490.00 500.00 510.00 520.00 530.00 540.00 550.00 560.00

C4H10O

ρ ± σ fit kg ⋅ m−3 652.75 ± 0.73 638.11 ± 0.75 623.10 ± 0.77 607.60 ± 0.80 591.23 ± 0.83 573.48 ± 0.88 553.60 ± 0.95 530.61 ± 1.05 503.20 ± 1.20 469.33 ± 1.43 424.91 ± 1.86 350.97 ± 2.78

MW = 74.12

6

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 1.8025 · 10−1 (combined temperature ranges, weighted), σc,uw = 4.7605 · 10−2 (combined temperature ranges, unweighted). Coefficient A B C

T = 273.15 to 348.95 K ρ = A + BT + CT 2 + DT 3 + … 8.60370 · 102 4.37482 · 10−1 −2.11090 · 10−3

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 3 −3 − in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 285.85 812.90 ± 0.60 −0.04 14-smi( ) 341.35 763.70 ± 0.70 −0.04 290.95 808.80 ± 0.60 −0.16 14-smi( ) 342.75 762.20 ± 0.70 −0.13 293.95 806.40 ± 0.60 −0.17 14-smi( ) 345.25 759.80 ± 0.70 0.00 295.95 804.70 ± 0.60 −0.26 14-smi( ) 347.45 757.50 ± 0.70 −0.04 313.45 790.40 ± 0.60 0.30 14-smi( ) 348.95 755.90 ± 0.70 −0.09 315.05 788.90 ± 0.60 0.22 14-smi( ) 273.15 822.71 ± 0.50 0.34 317.85 786.40 ± 0.60 0.24 14-smi( ) 288.15 810.87 ± 0.50 −0.29 320.35 783.90 ± 0.60 0.01 14-smi( ) 303.15 798.96 ± 0.50 −0.04 322.15 782.40 ± 0.60 0.17 14-smi( )

1)

Ref. (Symbol in Fig. 1)

14-smi( ) 14-smi( ) 14-smi( ) 14-smi( ) 14-smi( ) 28-tim/mar( ) 28-tim/mar( ) 28-tim/mar( )

Not included in Fig. 1.

cont.

Landolt-Börnstein New Series IV/8G

2.1.1 Alkanols, C1 - C4

31

ρ

ρ

Further references: [48-kor/pat].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ).

ρ ± σ fit kg ⋅ m−3

T K

270.00 280.00 290.00 293.15

824.61 ± 0.68 817.37 ± 0.60 809.71 ± 0.58 807.21 ± 0.59

l-2-Butanol

ρ ± σ fit kg ⋅ m−3

T K

803.16 ± 0.59 801.63 ± 0.60 793.13 ± 0.61 784.21 ± 0.62

298.15 300.00 310.00 320.00

[14898-79-4]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 51-ler/luc 804.2 ± 0.5

Landolt-Börnstein New Series IV/8G

T K

330.00 340.00 350.00 360.00 C4H10O

ρ ± σ fit kg ⋅ m−3 774.86 ± 0.64 765.09 ± 0.69 754.90 ± 0.80 744.29 ± 0.99 MW = 74.12

7

32

2.1.1 Alkanols, C1 - C4

(RS)-2-Butanol

[78-92-2]

C4H10O

MW = 74.12

8

Tc = 536.18 K [89-tej/lee] ρc = 276.00 kg·m−3 [89-tej/lee]

Table 1. Coefficients for the polynomial expansion equations. Standard deviations (see introduction): σ = 2.1049 (low temperature range), σc,w = (1.9422 combined temperature ranges, weighted), σc,uw = 8.1750 · 10−1 (combined temperature ranges, unweighted).

Coefficient

T = 200.00 to 410.00 K ρ = A + BT + CT 2 + DT 3 + …

1.16218 · 103 −2.35615 6.45589 · 10−3 −8.71602 · 10−6

A B C D

T = 410.00 to 536.18 K ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)] [ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] 4.61818 · 10−1 1.78871 · 10−3 −6.92823 · 10−5 3.07819 · 10−7

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 273.15 822.61 ± 0.20 −0.04 22-tim(◆) 433.15 667.70 ± 0.60 18.32 273.15 822.73 ± 0.15 0.08 28-tim/mar(∆) 453.15 636.50 ± 0.60 16.34 288.15 810.86 ± 0.15 0.10 6.20 28-tim/mar(∆) 293.15 812.90 ± 0.30 303.15 798.93 ± 0.15 0.54 9.71 28-tim/mar(∆) 407.23 694.40 ± 0.50 293.15 806.50 ± 0.20 −0.20 29-ber(✕ ) 424.02 670.10 ± 0.50 8.62 298.15 802.50 ± 0.15 −0.08 4.59 45-kol/bur(∇) 444.77 637.70 ± 0.50 293.15 807.30 ± 0.40 0.60 55-kus1) 453.55 623.30 ± 0.50 3.79 298.15 803.30 ± 0.40 0.72 55-kus1) 461.35 609.20 ± 0.50 3.07 303.15 799.10 ± 0.40 0.71 55-kus1) 473.25 587.10 ± 1.00 4.22 313.15 790.60 ± 0.40 0.82 55-kus1) 478.56 575.80 ± 1.00 4.53 323.15 781.70 ± 0.40 0.87 55-kus(✕ ) 494.70 539.00 ± 2.00 8.35 333.15 772.30 ± 0.50 0.82 55-kus1) 504.39 513.20 ± 3.00 11.41 343.15 762.20 ± 0.50 0.52 55-kus(✕ ) 302.75 798.80 ± 0.40 0.07 353.15 752.10 ± 0.50 0.73 55-kus(✕ ) 318.25 785.70 ± 0.40 0.44 213.15 866.80 ± 0.60 −2.07 58-cos/bow(✕ ) 332.35 772.10 ± 0.40 −0.14 233.15 851.70 ± 0.60 −1.62 58-cos/bow(✕ ) 347.75 756.70 ± 0.50 −0.30 253.15 837.20 ± 0.60 −0.85 58-cos/bow(✕ ) 362.15 740.90 ± 0.50 −0.73 273.15 822.10 ± 0.50 −0.55 58-cos/bow1) 200.00 875.00 ± 1.50 −4.46 293.15 806.00 ± 0.50 −0.70 58-cos/bow1) 220.00 862.00 ± 1.50 −1.49 313.15 789.40 ± 0.50 −0.38 58-cos/bow1) 240.00 846.00 ± 1.50 −2.08 333.15 771.40 ± 0.50 −0.08 58-cos/bow1) 260.00 830.00 ± 1.50 −2.81 353.15 753.90 ± 0.50 2.53 58-cos/bow(✕ ) 280.00 814.00 ± 1.50 −3.27 373.15 735.60 ± 0.60 6.56 58-cos/bow(✕ ) 300.00 798.00 ± 1.50 −3.04 393.15 716.90 ± 0.60 12.83 58-cos/bow1) 320.00 781.00 ± 1.50 −2.69 413.15 695.50 ± 0.60 19.33 58-cos/bow(✕ ) 340.00 761.00 ± 1.50 −3.82 1)

Ref. (Symbol in Fig. 1) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 63-amb/tow1) 63-amb/tow1) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-tho/mea1) 63-tho/mea(✕ ) 63-tho/mea(✕ ) 63-tho/mea(✕ ) 63-tho/mea(✕ ) 64-dan/bah(✕ ) 64-dan/bah(✕ ) 64-dan/bah(✕ ) 64-dan/bah(✕ ) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1)

Not included in Fig. 1.

cont.

Landolt-Börnstein New Series IV/8G

2.1.1 Alkanols, C1 - C4 Table 2. (cont.) ρexp − ρcalc ρexp ± 2σ est T −3 kg ⋅ m−3 K kg ⋅ m 360.00 742.00 ± 1.50 −2.00 380.00 717.00 ± 1.50 −3.81 400.00 693.00 ± 1.50 −1.84 420.00 667.00 ± 1.70 0.19 440.00 638.00 ± 1.70 −1.98 460.00 607.00 ± 2.00 −1.54 480.00 572.00 ± 2.00 4.02 500.00 532.00 ± 2.00 16.66 520.00 465.00 ± 3.00 20.36 293.15 806.61 ± 0.20 −0.09 298.15 802.44 ± 0.20 −0.14 303.15 798.25 ± 0.20 −0.14 320.00 783.42 ± 0.20 −0.27 340.00 764.17 ± 0.20 −0.65 360.00 742.98 ± 0.20 −1.02 380.00 719.83 ± 0.20 −0.98 400.00 694.75 ± 0.20 −0.09 1)

Ref. (Symbol in Fig. 1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah(✕ ) 64-dan/bah(✕ ) 64-dan/bah(✕ ) 76-hal/ell(✕ ) 76-hal/ell1) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ )

T K

420.00 440.00 460.00 483.83 490.00 293.15 293.15 353.15 353.15 298.15 313.15 293.15 313.15 323.15 333.15 298.15

33

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m

kg ⋅ m−3

−3

667.41 ± 0.20 637.44 ± 0.20 604.02 ± 0.25 557.48 ± 0.30 543.63 ± 0.30 807.70 ± 0.50 807.80 ± 0.50 755.80 ± 0.50 755.80 ± 0.50 802.50 ± 0.30 790.00 ± 0.30 806.66 ± 0.10 789.66 ± 0.10 780.46 ± 0.15 770.78 ± 0.15 802.49 ± 0.06

0.60 −2.54 −4.52 −1.44 0.27 1.00 1.10 4.43 4.43 −0.08 0.22 −0.04 −0.12 −0.37 −0.70 −0.09

Ref. (Symbol in Fig. 1) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 81-kor/kov1) 81-kor/kov1) 81-kor/kov(✕ ) 81-kor/kov(✕ ) 85-ogi/ara1) 85-ogi/ara(✕ ) 86-cha/lam( ) 86-cha/lam( ) 86-cha/lam( ) 86-cha/lam( ) 88-oka/oga( )

Not included in Fig. 1.

Further references: [1869-lie, 06-car/fer, 11-pic/ken, 13-pic/ken, 14-smi, 14-vav, 16-wil/bru, 19-beh, 19-eyk, 21-bru/cre, 21-rei/hic, 23-bru, 23-clo/joh, 25-fai, 25-nor/ash, 26-mun, 33-huc/ack, 33-nev/jat, 35-but/ram, 35-mah-1, 39-all/lin, 39-bar/atk, 39-lar/hun, 42-boe/han-1, 48-wei, 49-ber/ped, 50-pic/zie, 51-ami/wei, 51-bot, 52-coo, 52-dun/was, 56-rus/ame, 62-bro/smi, 63-mcc/lai, 65-fin/kid, 67-gol/per, 68-ano, 68-eva/lin, 69-bro/foc, 78-sac/pes, 80-cha/ses, 80-kas/izy, 80-rig/ube, 83-fuk/ogi, 85-rao/red, 86-kar/cam, 87-kri/cho, 88-nag-2, 89-nao/sur, 92-tan/mur, 94-ben/car, 96-bha/mak, 96-dej/gon-1, 98-fen/cho].

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

200.00 210.00 220.00 230.00 240.00 250.00 260.00 270.00 280.00 290.00 293.15 298.15

ρ ± σ fit kg ⋅ m−3 879.46 ± 1.58 871.38 ± 1.33 863.49 ± 1.11 855.74 ± 0.92 848.08 ± 0.76 840.45 ± 0.63 832.81 ± 0.52 825.10 ± 0.44 817.27 ± 0.38 809.27 ± 0.33 806.70 ± 0.32 802.58 ± 0.31

T K

300.00 310.00 320.00 330.00 340.00 350.00 360.00 370.00 380.00 390.00 400.00 410.00

ρ ± σ fit kg ⋅ m−3 801.04 ± 0.30 792.53 ± 0.29 783.69 ± 0.29 774.47 ± 0.29 764.82 ± 0.31 754.68 ± 0.33 744.00 ± 0.35 732.73 ± 0.38 720.81 ± 0.41 708.20 ± 0.44 694.84 ± 0.47 680.68 ± 0.51

T K

420.00 430.00 440.00 450.00 460.00 470.00 480.00 490.00 500.00 510.00 520.00 530.00

ρ ± σ fit kg ⋅ m−3 666.81 ± 0.60 653.58 ± 0.62 639.98 ± 0.64 625.17 ± 0.66 608.54 ± 0.70 589.60 ± 0.74 567.98 ± 0.81 543.36 ± 0.90 515.34 ± 1.05 483.12 ± 1.31 444.64 ± 1.82 391.57 ± 3.20 cont.

Landolt-Börnstein New Series IV/8G

34

2.1.1 Alkanols, C1 - C4

ρ

ρ

(RS)-2-Butanol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

2-Methyl-1-propanol

[78-83-1]

C4H10O

MW = 74.12

9

Tc = 547.74 K [63-amb/bro] ρc = 272.20 kg·m−3 [63-amb/bro] Table 1. Coefficients for the polynomial expansion equations. Standard deviations (see introduction): σ = 1.9234 (low temperature range), σc,w = (1.4721 combined temperature ranges, weighted), σc,uw = 8.2141 · 10−1 (combined temperature ranges, unweighted).

Coefficient

A B C D

T = 213.15 to 440.00 K ρ = A + BT + CT 2 + DT 3 + …

1.16796 · 103 −2.41227 6.24427 · 10−3 −7.77901 · 10−6

T = 440.00 to 547.74 K ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)] [ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] 8.96238 · 10−1 −1.28076 · 10−2 9.68824 · 10−5 −2.95139 · 10−7 cont.

Landolt-Börnstein New Series IV/8G

2.1.1 Alkanols, C1 - C4 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 273.15 816.22 ± 0.70 −0.18 1881-ber1) 273.15 819.60 ± 0.60 3.20 280.71 810.50 ± 0.70 −0.28 1881-ber1) 273.15 817.00 ± 0.60 0.60 281.64 809.80 ± 0.70 −0.29 1881-ber1) 380.15 726.00 ± 0.60 0.04 287.65 805.20 ± 0.70 −0.39 1881-ber1) 380.15 726.00 ± 0.60 0.04 290.95 802.70 ± 0.70 −0.40 1881-ber1) 273.15 817.03 ± 0.60 0.63 292.15 801.80 ± 0.70 −0.40 1881-ber1) 288.15 805.74 ± 0.60 0.53 292.25 801.70 ± 0.70 −0.42 1881-ber1) 303.15 794.35 ± 0.60 0.54 303.86 792.70 ± 0.70 −0.56 1881-ber1) 303.15 795.00 ± 0.45 1.19 304.40 792.30 ± 0.70 −0.54 1881-ber1) 313.15 788.90 ± 0.45 2.89 1) 310.44 787.20 ± 0.70 −0.94 1881-ber 323.15 778.80 ± 0.45 0.81 319.71 780.00 ± 0.70 −0.78 1881-ber1) 333.15 770.70 ± 0.45 0.98 319.86 779.90 ± 0.70 −0.75 1881-ber1) 348.15 754.50 ± 0.45 −2.22 333.85 768.00 ± 0.70 −1.13 1881-ber1) 273.15 817.20 ± 0.30 0.80 342.12 760.80 ± 1.00 −1.24 1881-ber1) 298.15 798.09 ± 0.30 0.45 354.01 749.70 ± 1.00 −1.72 1881-ber1) 293.15 802.10 ± 0.60 0.66 372.43 731.80 ± 1.00 −2.02 1881-ber(✕ ) 315.85 785.20 ± 0.60 1.34 372.63 731.50 ± 1.00 −2.12 1881-ber(✕ ) 334.65 769.90 ± 0.60 1.45 375.12 729.50 ± 1.00 −1.61 1881-ber(✕ ) 358.15 750.10 ± 0.60 2.51 379.75 726.50 ± 1.00 0.12 1883-sch-3(✕ ) 493.15 555.50 ± 0.50 −2.98 379.55 726.50 ± 1.00 −0.08 1884-sch-6(✕ ) 503.15 533.80 ± 0.50 −1.35 283.15 809.90 ± 0.50 0.94 1890-gar1) 513.15 503.20 ± 0.50 −5.19 293.15 801.90 ± 0.50 0.46 1890-gar1) 523.15 478.90 ± 0.60 2.36 303.15 794.00 ± 0.50 0.19 1890-gar1) 533.15 441.20 ± 2.00 4.89 313.15 786.50 ± 0.50 0.49 1890-gar1) 543.15 283.00 ± 3.00 −92.91 323.15 779.20 ± 0.50 1.21 1890-gar(✕ ) 547.74 269.00 ± 5.00 −3.20 273.15 816.96 ± 0.60 0.56 02-you/for(✕ ) 293.15 802.30 ± 0.50 0.86 289.50 804.59 ± 0.60 0.39 02-you/for1) 298.15 798.30 ± 0.50 0.66 289.40 806.78 ± 0.50 2.51 12-sch-31) 303.15 794.30 ± 0.50 0.49 304.95 794.21 ± 0.50 1.79 12-sch-31) 313.15 786.30 ± 0.50 0.29 326.15 776.49 ± 0.50 0.95 12-sch-3(✕ ) 323.15 778.50 ± 0.50 0.51 347.80 758.27 ± 0.70 1.24 12-sch-3(✕ ) 333.15 770.20 ± 0.50 0.48 1) 289.40 806.78 ± 0.50 2.51 15-sch-1 343.15 761.60 ± 0.50 0.46 304.95 794.21 ± 0.50 1.79 15-sch-11) 353.15 752.70 ± 0.50 0.49 326.15 776.49 ± 0.50 0.95 15-sch-1(✕ ) 293.15 801.60 ± 0.50 0.16 347.80 758.27 ± 0.70 1.24 15-sch-1(✕ ) 313.15 786.20 ± 0.50 0.19 201.65 885.00 ± 1.50 13.35 17-jae1) 333.15 769.60 ± 0.50 −0.12 261.15 828.00 ± 1.50 2.70 17-jae(✕ ) 213.15 861.30 ± 0.60 −0.85 273.45 817.00 ± 1.50 0.82 17-jae1) 233.15 846.40 ± 0.60 0.02 283.55 807.00 ± 1.50 −1.66 17-jae1) 253.15 831.40 ± 0.60 0.14 298.25 794.00 ± 1.50 −3.57 17-jae1) 273.15 816.70 ± 0.50 0.30 308.25 785.00 ± 1.50 −4.85 17-jae1) 293.15 802.10 ± 0.50 0.66 322.85 771.00 ± 1.50 −7.24 17-jae1) 313.15 785.80 ± 0.50 −0.21 342.75 753.00 ± 1.50 −8.49 17-jae1) 333.15 769.20 ± 0.50 −0.52 374.15 731.00 ± 1.50 −1.09 17-jae1) 353.15 751.00 ± 0.50 −1.21 1)

35

Ref. (Symbol in Fig. 1) 22-mic(✕ ) 26-han(✕ ) 27-arb-2(✕ ) 27-arb-2(✕ ) 28-tim/mar(✕ ) 28-tim/mar1) 28−tim/mar1) 33-azi/bha1) 33-azi/bha1) 33-azi/bha(✕ ) 33-azi/bha(✕ ) 33-azi/bha(✕ ) 45-alb/was(◆) 45-alb/was1) 48-vog-21) 48-vog-21) 48-vog-2(✕ ) 48-vog-2(✕ ) 55-kay/don(✕ ) 55-kay/don(✕ ) 55-kay/don(✕ ) 55-kay/don(✕ ) 55-kay/don(✕ ) 55-kay/don1) 55-kay/don(✕ ) 55-kus1) 55-kus1) 55-kus1) 55-kus1) 55-kus(✕ ) 55-kus(✕ ) 55-kus(✕ ) 55-kus(✕ ) 56-tor-11) 56-tor-11) 56-tor-1(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow1) 58-cos/bow1) 58-cos/bow(✕ ) 58-cos/bow(✕ )

Not included in Fig. 1.

cont.

Landolt-Börnstein New Series IV/8G

36

2.1.1 Alkanols, C1 - C4

2-Methyl-1-propanol (cont.)

Table 2. (cont.) ρexp − ρcalc ρexp ± 2σ est T −3 kg ⋅ m−3 K kg ⋅ m 373.15 731.30 ± 0.60 −1.80 393.15 711.50 ± 0.60 −0.52 413.15 689.00 ± 0.60 0.41 433.15 664.30 ± 0.60 1.85 293.15 802.20 ± 0.40 0.76 421.16 667.50 ± 0.50 −10.97 434.40 659.40 ± 0.50 −1.32 454.31 629.70 ± 0.50 −1.22 459.55 621.10 ± 0.50 −1.21 467.04 611.10 ± 0.50 1.65 476.88 594.30 ± 1.00 2.78 487.09 574.60 ± 1.00 3.23 497.04 553.90 ± 1.00 4.16 502.46 541.60 ± 1.00 4.74 509.32 523.90 ± 1.00 4.77 515.30 508.80 ± 1.00 6.76 521.85 488.80 ± 2.00 7.75 526.06 474.30 ± 3.00 8.38 535.44 431.30 ± 5.00 6.14 200.00 868.00 ± 1.50 −5.04 220.00 855.00 ± 1.50 −1.65 240.00 840.00 ± 1.50 −1.15 260.00 825.00 ± 1.50 −1.16 1)

Ref. (Symbol in Fig. 1) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 63-amb/tow1) 63-amb/tow1) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 64-dan/bah1) 64-dan/bah(✕ ) 64-dan/bah(✕ ) 64-dan/bah(✕ )

T K

280.00 300.00 320.00 340.00 360.00 380.00 400.00 420.00 440.00 460.00 480.00 500.00 520.00 540.00 298.15 303.15 298.15 298.15 298.15 303.15 308.15 313.15

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

810.00 ± 1.50 795.00 ± 1.50 778.00 ± 1.50 762.00 ± 1.50 743.00 ± 1.50 722.00 ± 1.50 700.00 ± 1.70 676.00 ± 1.70 650.00 ± 2.00 620.00 ± 2.00 590.00 ± 2.00 553.00 ± 2.00 510.00 ± 2.50 440.00 ± 6.00 794.35 ± 0.15 794.39 ± 0.20 797.87 ± 0.06 797.81 ± 0.10 798.30 ± 0.40 794.31 ± 0.40 790.26 ± 0.40 786.23 ± 0.40

−1.31 −1.23 −2.54 −1.88 −2.86 −4.12 −4.28 −3.96 −2.80 −1.55 4.46 10.18 22.74 40.84 −3.29 0.58 0.23 0.17 0.66 0.50 0.33 0.22

kg ⋅ m

Ref. (Symbol in Fig. 1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah(✕ ) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah(✕ ) 64-dan/bah(✕ ) 64-dan/bah(✕ ) 64-dan/bah(✕ ) 80-kas/izy(∆) 86-mou/nai(∇) 88-oka/oga( ) 96-dom/rod( ) 98-nik/shi1) 98-nik/shi1) 98-nik/shi1) 98-nik/shi(✕ )

Not included in Fig. 1.

Further references: [1872-lin/von-2, 1872-pie/puc, 1884-gla, 1884-per, 1891-jah, 1891-sch/kos, 1892-lan/jah, 1894-jah/mol, 1898-kah, 08-dor/dvo, 11-dor, 13-rom, 14-eng/tur, 14-gas, 14-wor, 15-pea, 15-ric/coo, 16-wro/rei, 19-eyk, 21-bru/cre, 21-rei/hic, 23-pop, 23-wil/smi, 25-nor/ash, 26-mat, 26-mun, 31-sto/hul, 32-byl, 33-huc/ack, 33-tre/wat, 33-vos/con, 34-smi, 35-but/ram, 35-mah-1, 39-all/lin, 39-lar/hun, 42-sny/gil, 43-boh, 46-fri/sto, 47-sho/pri, 48-wei, 50-cro/van, 50-mum/phi, 50-pic/zie, 51-hau, 51-tei/gor, 52-coo, 52-dun/was, 53-ani, 53-ani-1, 53-hag/dec, 53-par/cha, 55-dan/col, 56-rus/ame, 58-ano-5, 62-bro/smi, 63-mcc/lai, 67-gol/per, 67-nat/rao, 68-ano, 69-bro/foc, 69-smi/kur, 70-sus/hol, 82-ber/rog-1, 82-kar/red, 82-ven/dha, 83-fuk/ogi, 83-lin, 84-ber/pen, 85-mat/ben, 85-mat/ben-1, 85-rao/red, 87-ber-1, 87-kri/cho, 88-nag, 88-nag-1, 90-mal/rao, 92-kum/sre, 93-ami/rai, 95-red/ram-1, 96-bha/mak, 96-nik/jad, 96-nik/mah, 98-art/dom, 98-sen].

cont.

Landolt-Börnstein New Series IV/8G

37

ρ

ρ

2.1.1 Alkanols, C1 - C4

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

210.00 220.00 230.00 240.00 250.00 260.00 270.00 280.00 290.00 293.15 298.15 300.00

Landolt-Börnstein New Series IV/8G

ρ ± σ fit kg ⋅ m−3 864.71 ± 1.50 856.65 ± 1.26 848.81 ± 1.05 841.15 ± 0.88 833.61 ± 0.75 826.16 ± 0.65 818.74 ± 0.57 811.31 ± 0.52 803.82 ± 0.50 801.44 ± 0.49 797.64 ± 0.49 796.23 ± 0.49

T K

310.00 320.00 330.00 340.00 350.00 360.00 370.00 380.00 390.00 400.00 410.00 420.00

ρ ± σ fit kg ⋅ m−3 788.48 ± 0.49 780.54 ± 0.52 772.36 ± 0.55 763.88 ± 0.59 755.06 ± 0.63 745.86 ± 0.67 736.23 ± 0.71 726.12 ± 0.75 715.48 ± 0.78 704.28 ± 0.80 692.45 ± 0.82 679.96 ± 0.83

T K

430.00 440.00 450.00 460.00 470.00 480.00 490.00 500.00 510.00 520.00 530.00 540.00

ρ ± σ fit kg ⋅ m−3 666.76 ± 0.83 652.80 ± 0.84 637.78 ± 0.97 621.55 ± 1.00 604.19 ± 1.03 585.54 ± 1.08 565.28 ± 1.14 542.82 ± 1.22 517.27 ± 1.35 487.26 ± 2.55 450.24 ± 3.89 399.16 ± 4.57

38

2.1.1 Alkanols, C1 - C4

2-Methyl-2-propanol

[75-65-0]

C4H10O

MW = 74.12

10

Tc = 506.20 K [89-tej/lee] ρc = 270.00 kg·m−3 [89-tej/lee]

Table 1. Coefficients for the polynomial expansion equations. Standard deviations (see introduction): σ = 4.8919 (low temperature range), σc,w = (1.7560 combined temperature ranges, weighted), σc,uw = 4.6459 · 10−1 (combined temperature ranges, unweighted).

Coefficient

T = 273.15 to 400.00 K ρ = A + BT + CT 2 + DT 3 + …

9.06345 · 102 1.53910 · 10−1 −1.93019 · 10−3

A B C D

T = 400.00 to 506.20 K ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)] [ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] 1.32387 −2.89194 · 10−2 2.93882 · 10−4 −1.07285 · 10−6

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 273.15 807.40 ± 1.00 3.03 1872-but(✕ ) 447.23 575.40 ± 0.50 2.89 1) 303.15 775.40 ± 1.00 −0.22 1872-but 456.20 556.10 ± 0.50 2.63 303.15 777.50 ± 0.50 1.88 31-smy/dor-11) 465.81 533.00 ± 0.50 2.08 323.15 756.30 ± 0.50 1.78 31-smy/dor-11) 473.52 512.80 ± 1.00 2.70 343.15 734.30 ± 0.50 2.42 31-smy/dor-1(✕ ) 480.56 490.50 ± 1.00 2.68 293.15 786.68 ± 0.50 1.09 34-tim/del(◆) 300.00 776.00 ± 1.50 −2.80 303.15 776.18 ± 0.50 0.56 34-tim/del1) 320.00 756.00 ± 1.50 −1.94 308.15 770.88 ± 0.50 0.39 34-tim/del1) 340.00 736.00 ± 1.50 0.46 313.15 765.58 ± 0.50 0.32 34-tim/del1) 360.00 712.00 ± 1.50 0.40 298.15 781.60 ± 0.40 0.95 55-kus1) 380.00 686.00 ± 1.50 −0.11 303.15 776.60 ± 0.40 0.98 55-kus1) 400.00 654.00 ± 1.50 −5.08 313.15 766.50 ± 0.40 1.24 55-kus1) 420.00 618.00 ± 1.70 −7.60 1) 323.15 755.90 ± 0.40 1.38 55-kus 440.00 580.00 ± 1.70 −7.09 333.15 741.50 ± 0.50 −1.89 55-kus1) 460.00 536.00 ± 2.00 −8.90 343.15 734.20 ± 0.50 2.32 55-kus(✕ ) 480.00 476.00 ± 2.50 −13.74 353.15 722.60 ± 0.50 2.63 55-kus(✕ ) 500.00 380.00 ± 6.00 −11.52 313.15 765.20 ± 0.50 −0.06 58-cos/bow1) 300.65 778.10 ± 0.12 −0.05 333.15 742.90 ± 0.50 −0.49 58-cos/bow1) 303.15 775.43 ± 0.12 −0.19 353.15 721.20 ± 0.50 1.23 58-cos/bow(✕ ) 308.15 770.23 ± 0.12 −0.26 373.15 697.40 ± 0.50 2.38 58-cos/bow(✕ ) 313.15 757.60 ± 0.15 −7.66 393.15 671.50 ± 0.60 2.99 58-cos/bow(✕ ) 340.00 735.05 ± 0.15 −0.49 413.15 645.00 ± 0.60 6.98 58-cos/bow(✕ ) 360.00 710.82 ± 0.17 −0.78 300.15 779.20 ± 0.40 0.55 63-amb/tow1) 380.00 684.41 ± 0.17 −1.70 419.82 628.10 ± 0.50 2.16 63-amb/tow(✕ ) 400.00 655.47 ± 0.17 −3.61 433.61 603.50 ± 0.50 3.85 63-amb/tow(✕ ) 420.00 623.36 ± 0.20 −2.24 1)

Ref. (Symbol in Fig. 1) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah(✕ ) 83-hal/gun(∇) 83-hal/gun(∇) 83-hal/gun(∇) 83-hal/gun(∇) 83-hal/gun(∇) 83-hal/gun(∇) 83-hal/gun(∇) 83-hal/gun(∇) 83-hal/gun(∇)

Not included in Fig. 1.

cont.

Landolt-Börnstein New Series IV/8G

2.1.1 Alkanols, C1 - C4 Table 2. (cont.) ρexp − ρcalc ρexp ± 2σ est T −3 kg ⋅ m−3 K kg ⋅ m 440.00 587.07 ± 0.20 −0.02 450.00 566.74 ± 0.20 −0.03 460.00 544.38 ± 0.20 −0.52 465.00 532.21 ± 0.20 −0.73 303.15 775.46 ± 0.15 −0.16 333.15 743.18 ± 0.15 −0.21 303.15 775.21 ± 0.10 −0.41 1)

Ref. (Symbol in Fig. 1) 83-hal/gun(∇) 83-hal/gun(∇) 83-hal/gun(∇) 83-hal/gun(∇) 87-pik1) 87-pik(∆) 88-kim/mar( )

T K

308.15 313.15 318.15 323.15 328.15 299.15

39

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m

kg ⋅ m−3

−3

769.97 ± 0.10 764.69 ± 0.10 759.37 ± 0.10 754.01 ± 0.10 748.61 ± 0.10 779.48 ± 0.15

−0.52 −0.57 −0.57 −0.51 −0.39 −0.17

Ref. (Symbol in Fig. 1)

) ) ) ) ) )

88-kim/mar( 88-kim/mar( 88-kim/mar( 88-kim/mar( 88-kim/mar( 88-oka/oga(

Not included in Fig. 1.

ρ

ρ

Further references: [1872-lin/von-2, 1880-bru-1, 1884-per, 1893-tho/jon, 02-you/for, 06-car/fer, 08-ric/mat, 11-dor-1, 19-beh, 19-eyk, 25-nor/ash, 26-mun, 29-pre, 29-swa, 33-gin/her, 33-nev/jat, 35-hen, 36-ipa/cor, 36-spe, 39-owe/qua, 44-ira, 46-sim/was, 48-wei, 49-dre/mar, 50-pic/zie, 52-dun/was, 54-wes/aud, 55-bou/cle, 55-wes, 56-rus/ame, 62-bro/smi, 63-mcc/lai, 69-bro/foc, 70-sus/hol, 71-des/bha-1, 76-tri/kri, 77-gov/and-1, 80-kas/izy, 83-pik-2, 85-rao/red, 87-kri/cho, 88-cac/cos, 95-red/ram-1, 96-bha/mak, 96-nik/mah, 98-nik/shi].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont. Landolt-Börnstein New Series IV/8G

40

2.1.1 Alkanols, C1 - C4

2-Methyl-2-propanol (cont.) Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15 300.00 310.00 320.00 330.00

ρ ± σ fit kg ⋅ m−3 807.19 ± 1.50 798.11 ± 1.20 788.65 ± 1.13 785.59 ± 1.00 780.65 ± 0.91 778.80 ± 0.80 768.57 ± 0.75 757.94 ± 0.70 746.94 ± 0.60

T K

340.00 350.00 360.00 370.00 380.00 390.00 400.00 410.00 420.00

ρ ± σ fit kg ⋅ m−3 735.54 ± 0.72 723.77 ± 0.90 711.60 ± 1.22 699.05 ± 1.51 686.11 ± 1.74 672.79 ± 2.00 659.08 ± 2.30 643.47 ± 2.60 625.60 ± 2.90

T K

430.00 440.00 450.00 460.00 470.00 480.00 490.00 500.00

ρ ± σ fit kg ⋅ m−3 606.64 ± 3.20 587.09 ± 3.53 566.77 ± 3.80 544.90 ± 4.10 519.99 ± 4.40 489.74 ± 4.70 450.24 ± 5.00 391.52 ± 5.32

Landolt-Börnstein New Series IV/8G

2.1.2 Alkanols, C5 - C6

41

2.1.2 Alkanols, C5 - C6 2,2-Dimethyl-1-propanol

[75-84-3]

C5H12O

MW = 88.15

11

C5H12O

MW = 88.15

12

Table 1. Experimental value with uncertainty. T K 303.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

799.0 ± 0.3

74-mye/cle

2-Methyl-1-butanol

[137-32-6]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 7.9216 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.8175 · 10−1 (combined temperature ranges, unweighted). T = 293.15 to 390.65 K ρ = A + BT + CT 2 + DT 3 + … 1.00094 · 103 −4.27416 · 10−1 −6.53533 · 10−4

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

298.15 296.15 293.15 293.15 308.15 293.15 293.15 298.15 302.65 324.35 337.95 353.05 1)

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

815.20 ± 0.50 816.00 ± 1.00 819.30 ± 0.60 818.44 ± 1.00 807.40 ± 1.00 820.00 ± 1.00 819.80 ± 1.00 815.00 ± 1.00 811.10 ± 0.50 792.80 ± 0.50 781.40 ± 0.50 768.70 ± 0.50

−0.21 −1.04 −0.18 −1.04 0.23 0.52 0.32 −0.41 −0.62 −0.75 −0.45 0.12

kg ⋅ m

Ref. (Symbol in Fig. 1)

27-nor/cor( ) 31-lev/mar-4(✕ ) 37-bra(◆) 38-whi/ole(✕ ) 46-haf/lov(✕ ) 51-lyu/ter(✕ ) 52-coo(✕ ) 56-ike/kep(✕ ) 63-tho/mea(∇) 63-tho/mea(∇) 63-tho/mea(∇) 63-tho/mea(∇)

T K

367.95 378.15 390.65 293.15 298.15 293.15 298.15 303.15 313.15 323.15 333.15 343.15

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

754.90 ± 0.50 745.10 ± 0.55 734.30 ± 0.55 818.80 ± 0.50 814.80 ± 0.30 819.80 ± 1.00 815.90 ± 1.00 812.40 ± 1.00 804.60 ± 1.50 796.80 ± 1.50 788.80 ± 1.50 780.10 ± 1.50

−0.29 −0.75 0.07 −0.68 −0.61 0.32 0.49 1.10 1.60 2.23 2.79 2.79

kg ⋅ m

Ref. (Symbol in Fig. 1) 63-tho/mea(∇) 63-tho/mea(∇) 63-tho/mea(∇) 68-ano(∆) 82-dap/don( ) 83-fuk/ogi(✕ ) 83-fuk/ogi(✕ ) 83-fuk/ogi(✕ ) 83-fuk/ogi(✕ ) 83-fuk/ogi(✕ ) 83-fuk/ogi1) 83-fuk/ogi1)

Not included in Fig. 1.

Further references: [1884-per, 01-mar/mck, 16-wil/bru, 33-tre/wat, 35-gui, 37-gin/bau, 39-bar/atk, 48-bro/bro, 48-wei, 50-pic/zie, 52-hel, 63-mcc/lai]

cont.

Landolt-Börnstein New Series IV/8G

42

2.1.2 Alkanols, C5 - C6

ρ

ρ

2-Methyl-1-butanol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

290.00 293.15 298.15 300.00 310.00

ρ ± σ fit kg ⋅ m−3 822.02 ± 0.95 819.48 ± 0.92 815.41 ± 0.90 813.89 ± 0.90 805.63 ± 0.98

(S)-(-)-2-Methyl-1-butanol

ρ ± σ fit kg ⋅ m−3

T K

797.24 ± 0.97 788.72 ± 0.89 780.07 ± 0.78 771.28 ± 0.65 762.37 ± 0.54

320.00 330.00 340.00 350.00 360.00

[1565-80-6]

T K

370.00 380.00 390.00 400.00

C5H12O

ρ ± σ fit kg ⋅ m−3 753.32 ± 0.49 744.15 ± 0.54 734.84 ± 0.73 725.40 ± 1.06

MW = 88.15

13

Table 1. Fit with estimated B coefficient for 7 accepted points. Deviation σw = 0.464. Coefficient ρ = A + BT 1047.24 A B −0.780 cont. Landolt-Börnstein New Series IV/8G

2.1.2 Alkanols, C5 - C6

43

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

293.15 293.15 300.65 293.15

ρexp ± 2σ est

ρexp − ρcalc kg ⋅ m

kg ⋅ m

818.9 ± 0.5 818.8 ± 0.6 813.0 ± 2.0 818.4 ± 1.0

T K

Ref.

−3

−3

0.32 0.18 0.27 −0.16

38-whi/ole 38-whi/ole-1 38-whi/ole-1 38-whi/ole-1

ρexp ± 2σ est −3

kg ⋅ m

293.15 818.3 ± 1.0 296.15 814.0 ± 1.5 289.15 821.6 ± 0.5

ρexp − ρcalc

Ref.

kg ⋅ m−3

−0.29 −2.24 −0.10

38-whi/ole-1 52-hel 59-pin/lar

Table 3. Recommended values. ρexp ± 2σ est

T K 280.00 290.00 293.15 298.15 310.00

kg ⋅ m−3

828.8 ± 1.6 821.0 ± 1.0 818.6 ± 1.0 814.7 ± 1.2 805.4 ± 2.1

2-Methyl-2-butanol

[75-85-4]

C5H12O

MW = 88.15

14

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 1.1040 (combined temperature ranges, weighted), σc,uw = 2.1679 · 10−1 (combined temperature ranges, unweighted). Coefficient A B C

T = 268.15 to 453.15 K ρ = A + BT + CT 2 + DT 3 + … 9.31063 · 102 6.74937 · 10−2 −1.64419 · 10−3

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

374.75 375.15 273.15 288.15 298.15 273.15 288.15 303.15 298.15 273.15 273.15 298.15 1)

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

724.10 ± 1.00 724.10 ± 1.00 827.00 ± 0.60 813.80 ± 0.50 804.73 ± 0.50 827.16 ± 0.60 813.44 ± 0.60 799.72 ± 0.60 805.99 ± 0.60 826.20 ± 2.00 826.20 ± 0.50 801.80 ± 0.50

−1.35 −0.88 0.18 −0.19 −0.30 0.34 −0.55 −0.70 0.96 −0.62 −0.62 −3.23

Ref. (Symbol in Fig. 1) 1883-sch-3(✕ ) 1884-sch-6(✕ ) 10-ric(✕ ) 27-nor/reu(✕ ) 27-nor/reu1) 32-tim/hen(✕ ) 32-tim/hen(✕ ) 32-tim/hen1) 35-but/ram( ) 39-owe/qua1) 39-owe/qua(✕ ) 39-owe/qua1)

T K

298.15 308.15 318.15 328.15 328.15 338.15 273.15 293.15 313.15 333.15 353.15 373.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

801.80 ± 2.00 792.30 ± 2.00 782.70 ± 2.00 773.10 ± 2.00 773.10 ± 2.00 762.40 ± 0.50 825.00 ± 0.50 808.40 ± 0.50 790.00 ± 0.50 771.30 ± 0.50 750.40 ± 0.50 728.10 ± 0.50

−3.23 −3.44 −3.41 −3.06 −3.06 −3.48 −1.82 −1.15 −0.96 0.24 0.56 0.79

Ref. (Symbol in Fig. 1) 39-owe/qua1) 39-owe/qua1) 39-owe/qua1) 39-owe/qua(✕ ) 39-owe/qua1) 39-owe/qua1) 58-cos/bow(✕ ) 58-cos/bow1) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ )

Not included in Fig.

cont.

Landolt-Börnstein New Series IV/8G

44

2.1.2 Alkanols, C5 - C6

2-Methyl-2-butanol (cont.) Table 2. (cont.) ρexp ± 2σ est

T K

1)

−3

kg ⋅ m

704.50 ± 0.50 679.40 ± 1.00 653.00 ± 1.00 623.90 ± 1.00 799.73 ± 0.25 806.70 ± 0.50 833.20 ± 0.50 822.60 ± 0.50

1.04 1.10 1.18 −0.12 −0.69 1.67 2.26 -0.03

kg ⋅ m

393.15 413.15 433.15 453.15 303.15 298.15 268.15 278.15

ρexp − ρcalc

−3

Ref. (Symbol in Fig. 1) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 75-hsu/cle(∇) 82-dap/don(◆) 85-dap/don(✕ ) 85-dap/don(✕ )

T K

298.15 308.15 298.15 298.15 303.15 308.15 313.15

ρexp ± 2σ est

ρexp − ρcalc

−3

kg ⋅ m

Ref. (Symbol in Fig. 1)

806.90 ± 0.50 796.20 ± 0.50 804.37 ± 0.60 805.00 ± 0.20 800.60 ± 0.20 796.00 ± 0.20 791.20 ± 0.20

1.87 0.46 −0.66 −0.03 0.18 0.26 0.24

85-dap/don1) 85-dap/don1) 85-tre/ben(∆) 86-rig/mar( ) 86-rig/mar( ) 86-rig/mar( ) 86-rig/mar( )

kg ⋅ m

−3

Not included in Fig. 1.

ρ

ρ

Further references: [1878-wis, 1884-per, 1893-tho/jon, 19-eyk, 26-mun, 33-nev/jat, 35-mah-1, 36-par, 37-gin/bau, 48-wei, 50-pic/zie, 51-lev/fai, 52-coo, 55-soe/fre, 57-pet/sus, 58-pan/osi, 63-mcc/lai, 67-gol/per, 76-tri/kri, 88-cab/bar, 96-nik/jad, 98-pai/che, 98-sen].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont.

Landolt-Börnstein New Series IV/8G

2.1.2 Alkanols, C5 - C6

45

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ).

ρ ± σ fit kg ⋅ m−3

T K

T K

837.46 ± 0.36 829.43 ± 0.37 821.06 ± 0.41 812.36 ± 0.46 809.55 ± 0.47 805.03 ± 0.50 803.33 ± 0.52 793.98 ± 0.58

260.00 270.00 280.00 290.00 293.15 298.15 300.00 310.00

320.00 330.00 340.00 350.00 360.00 370.00 380.00 390.00

3-Methyl-1-butanol

ρ ± σ fit kg ⋅ m−3 784.30 ± 0.64 774.28 ± 0.71 763.94 ± 0.77 753.27 ± 0.84 742.27 ± 0.90 730.95 ± 0.96 719.29 ± 1.02 707.30 ± 1.08

[123-51-3]

ρ ± σ fit kg ⋅ m−3

T K

400.00 410.00 420.00 430.00 440.00 450.00 460.00

C5H12O

694.99 ± 1.15 682.35 ± 1.21 669.38 ± 1.27 656.07 ± 1.34 642.45 ± 1.41 628.49 ± 1.49 614.20 ± 1.57

MW = 88.15

15

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 9.8281 · 10−1 (combined temperature ranges, weighted), σc,uw = 2.2532 · 10−1 (combined temperature ranges, unweighted). T = 273.15 to 347.85 K ρ = A + BT + CT 2 + DT 3 + … 8.89389 · 102 1.88877 · 10−1 −1.56150 · 10−3

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

285.45 307.15 327.15 347.85 293.15 293.15 273.15 288.15 303.15 293.15 313.15 333.15 293.15 1)

ρexp ± 2σ est

ρexp − ρcalc

−3

kg ⋅ m

Ref. (Symbol in Fig. 1)

815.83 ± 0.00 799.79 ± 0.50 783.63 ± 0.50 767.20 ± 0.50 810.50 ± 0.50 810.20 ± 0.50 823.88 ± 0.50 812.87 ± 1.00 801.73 ± 1.00 808.60 ± 2.00 793.80 ± 2.00 778.10 ± 1.00 811.57 ± 0.50

−0.24 −0.30 −0.43 1.05 −0.07 −0.37 −0.60 −1.29 −1.42 −1.97 −1.61 −0.90 1.00

11-sch1) 11-sch(✕ ) 11-sch(✕ ) 11-sch(✕ ) 26-mat(✕ ) 28-mon(✕ ) 29-tim/hen(∆) 29-tim/hen1) 29-tim/hen1) 56-tor-11) 56-tor-11) 56-tor-1(✕ ) 81-joo/arl(◆)

kg ⋅ m

−3

T K

303.15 303.15 298.15 303.15 308.15 313.15 303.15 298.15 298.15 303.15 308.15 298.15

ρexp ± 2σ est −3

kg ⋅ m

804.19 ± 0.30 801.77 ± 0.30 807.10 ± 0.20 802.70 ± 0.20 799.00 ± 0.20 794.90 ± 0.20 801.78 ± 1.00 806.90 ± 0.20 806.90 ± 0.20 803.00 ± 0.20 799.30 ± 0.20 807.10 ± 0.30

ρexp − ρcalc kg ⋅ m−3

1.04 −1.38 0.20 −0.45 −0.32 −0.51 −1.37 0.00 0.00 −0.15 −0.02 0.20

Ref. (Symbol in Fig. 1) 85-rao/red(✕ ) 86-mou/nai(✕ ) 86-rig/mar( ) 86-rig/mar( ) 86-rig/mar( ) 86-rig/mar( ) 92-kum/sre(✕ ) 92-tan/mur(✕ ) 93-ami/rai(∇) 93-ami/rai(∇) 93-ami/rai(∇) 98-sen(✕ )

Not included in Fig. 1.

cont.

Landolt-Börnstein New Series IV/8G

46

2.1.2 Alkanols, C5 - C6

3-Methyl-1-butanol (cont.)

ρ

ρ

Further references: [1876-bal, 1884-per, 1884-sch-6, 1886-tra, 1891-sch/kos, 1893-tho/jon, 1898-kah, 04-bru/sch, 07-che-1, 08-ric/mat, 13-muc, 14-eng/tur, 16-wro/rei, 21-rei/hic, 23-pop, 26-han, 26-mun, 27-krc/wil, 27-nor/cor, 28-har-2, 28-llo/bro, 33-nev/jat, 35-but/ram, 35-cou/hop, 35-mah-1, 36-spe, 36-tom, 37-gin/bau, 41-hus/age, 42-boh, 42-mul, 43-boh, 45-add, 48-vog-2, 48-wei, 49-udo/kal, 50-pic/zie, 52-coo, 53-par/cha, 56-ike/kep, 57-ano-1, 57-pet/sus, 57-rom-1, 58-arn/was, 60-ter/kep, 63-mcc/lai, 63-raj/ran, 65-red/rao, 67-gol/per, 68-ana/rao, 68-ano, 71-abr/ber, 71-tha/rao, 79-sub/rao, 82-dap/don, 82-kar/red, 87-isl/qua].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15

ρ ± σ fit kg ⋅ m−3 826.55 ± 0.22 819.85 ± 0.17 812.84 ± 0.22 810.57 ± 0.24

T K

298.15 300.00 310.00 320.00

ρ ± σ fit kg ⋅ m−3 806.90 ± 0.29 805.52 ± 0.31 797.88 ± 0.41 789.93 ± 0.51

T K

330.00 340.00 350.00 360.00

ρ ± σ fit kg ⋅ m−3 781.67 ± 0.61 773.10 ± 0.72 764.21 ± 0.84 755.01 ± 0.98

Landolt-Börnstein New Series IV/8G

2.1.2 Alkanols, C5 - C6 3-Methyl-2-butanol

[598-75-4]

47 C5H12O

MW = 88.15

16

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 7.5344 · 10−1 (combined temperature ranges, weighted), σc,uw = 2.8698 · 10−1 (combined temperature ranges, unweighted). Coefficient A B C

T = 293.15 to 378.15 K ρ = A + BT + CT 2 + DT 3 + … 8.82581 · 102 3.69971 · 10−1 −2.00997 · 10−3

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 293.15 293.15 293.15 298.15 302.55 1)

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

818.00 ± 0.50 818.20 ± 0.50 820.00 ± 1.00 815.00 ± 1.00 810.70 ± 0.50

−0.31 −0.11 1.69 0.79 0.17

Ref. (Symbol in Fig. 1)

12-pic/ken( ) 50-pic/zie( ) 63-tho/mea(∆) 63-tho/mea(∆) 63-tho/mea(∆)

T K 324.35 337.95 353.05 367.95 378.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

790.10 ± 0.50 777.80 ± 0.50 759.80 ± 0.50 746.10 ± 0.50 734.60 ± 0.55

−1.03 −0.25 −2.87 −0.49 −0.47

Ref. (Symbol in Fig. 1) 63-tho/mea(∆) 63-tho/mea(∆) 63-tho/mea1) 63-tho/mea(∆) 63-tho/mea(∆)

Not included in Fig. 1.

ρ ρ

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont. Landolt-Börnstein New Series IV/8G

48

2.1.2 Alkanols, C5 - C6

3-Methyl-2-butanol (cont.)

Further references: [1876-mun, 1878-win, 1878-wis, 33-ste, 37-gin/bau, 38-whi/joh, 48-mcm/rop, 52-coo, 63-mcc/lai].

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ).

ρ ± σ fit kg ⋅ m−3

T K

820.83 ± 0.59 818.31 ± 0.58 814.21 ± 0.57 812.68 ± 0.57 804.11 ± 0.58

290.00 293.15 298.15 300.00 310.00

ρ ± σ fit kg ⋅ m−3

T K

795.15 ± 0.60 785.79 ± 0.60 776.02 ± 0.59 765.85 ± 0.56 755.28 ± 0.55

320.00 330.00 340.00 350.00 360.00

(S)-3-Methyl-2-butanol

T K

[500029-41-4]

370.00 380.00 390.00

ρ ± σ fit kg ⋅ m−3 744.31 ± 0.57 732.93 ± 0.67 721.15 ± 0.86

C5H12O

MW = 88.15

17

C5H12O

MW = 88.15

18

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

810.0 ± 2.0

33-ste

1-Pentanol

[71-41-0]

Tc = 588.00 K [89-tej/lee] ρc = 270.00 kg·m−3 [89-tej/lee]

Table 1. Coefficients for the polynomial expansion equations. Standard deviations (see introduction): σ = 7.5696 · 10−1 (low temperature range), σc,w = (6.3480 · 10−1 combined temperature ranges, weighted), σc,uw = 3.3635 · 10−1 (combined temperature ranges, unweighted).

Coefficient

A B C D

T = 213.15 to 470.00 K ρ = A + BT + CT 2 + DT 3 + …

1.10034 · 103 −1.58026 · 100 3.34384 · 10−3 −4.34342 · 10−6

T = 470.00 to 588.00 K ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)] [ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] 1.06991 · 100 −1.91438 · 10−2 1.56345 · 10−4 −4.63597 · 10−7

cont. Landolt-Börnstein New Series IV/8G

2.1.2 Alkanols, C5 - C6

49

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 273.15 273.15 298.15 213.15 233.15 253.15 273.15 293.15 313.15 333.15 353.15 373.15 393.15 413.15 433.15 453.15 273.15 273.15 293.15 313.15 333.15 353.15 373.15 393.15 413.15 433.15 453.15 473.15 493.15 513.15 533.15 553.15 563.15 568.15 573.15 578.15 583.15 584.15 585.15 293.15 298.15 303.15 320.00 340.00 360.00 380.00 1)

ρexp ± 2σ est −3

kg ⋅ m

ρexp − ρcalc −3

kg ⋅ m

829.60 ± 0.50 −0.06 829.61 ± 0.20 −0.05 0.28 811.59 ± 0.20 873.00 ± 1.00 −0.36 858.10 ± 1.00 −0.52 843.00 ± 1.00 −1.12 827.80 ± 1.00 −1.86 813.30 ± 1.00 −1.72 798.10 ± 1.00 −1.91 783.40 ± 1.00 −1.00 0.00 768.00 ± 1.00 0.91 751.50 ± 1.00 3.64 735.60 ± 2.00 6.48 718.40 ± 2.00 8.06 698.30 ± 2.00 8.68 675.40 ± 2.00 1.17 830.83 ± 0.10 1.34 831.00 ± 1.50 815.00 ± 1.50 −0.02 800.00 ± 1.50 −0.01 780.00 ± 1.50 −4.40 784.00 ± 1.50 16.00 1.41 752.00 ± 1.50 0.04 732.00 ± 1.50 0.08 712.00 ± 1.50 690.00 ± 1.50 −0.24 665.00 ± 1.50 −1.72 640.00 ± 1.50 −1.11 612.00 ± 1.50 −0.01 0.43 581.00 ± 1.50 545.00 ± 1.50 −0.47 500.00 ± 2.00 −0.71 471.00 ± 2.00 −0.02 0.84 454.00 ± 2.00 1.63 434.00 ± 3.00 2.82 410.00 ± 3.00 365.00 ± 5.00 −8.61 350.00 ± 5.00 −14.84 324.00 ± 5.00 −30.71 814.45 ± 0.20 −0.57 810.80 ± 0.20 −0.51 807.12 ± 0.20 −0.46 794.46 ± 0.20 −0.28 778.81 ± 0.20 −0.07 762.11 ± 0.20 −0.05 -0.11 744.25 ± 0.20

Ref. (Symbol in Fig. 1) 26-han(✕ ) 32-ell/rei(✕ ) 32-ell/rei1) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow(✕ ) 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 59-mck/ski(∆) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr1) 76-hal/ell(✕ ) 76-hal/ell1) 76-hal/ell1) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ )

T K 400.00 420.00 440.00 460.00 470.00 480.00 490.00 288.15 298.15 308.15 318.15 303.15 313.15 298.15 308.15 318.15 333.15 278.15 288.15 298.15 308.15 318.15 298.15 268.15 278.15 298.15 308.15 298.15 303.15 308.15 313.15 323.15 328.15 333.15 338.15 343.15 348.15 353.15 358.15 363.15 373.15 278.15 288.15 298.15 308.15

ρexp ± 2σ est −3

kg ⋅ m

724.98 ± 0.20 704.25 ± 0.20 681.80 ± 0.25 657.53 ± 0.25 644.61 ± 0.30 631.11 ± 0.30 616.92 ± 0.30 818.20 ± 0.30 810.90 ± 0.30 803.90 ± 0.30 796.00 ± 0.30 807.58 ± 0.20 799.92 ± 0.20 810.97 ± 0.15 803.61 ± 0.15 796.05 ± 0.15 784.44 ± 0.15 825.34 ± 0.20 818.21 ± 0.20 811.34 ± 0.20 803.50 ± 0.20 795.83 ± 0.20 810.86 ± 0.10 839.00 ± 0.50 825.30 ± 0.50 810.90 ± 0.50 803.90 ± 0.50 811.00 ± 0.20 807.30 ± 0.20 803.90 ± 0.20 799.90 ± 0.20 792.18 ± 0.10 788.92 ± 0.10 784.39 ± 0.10 780.59 ± 0.10 776.19 ± 0.10 771.92 ± 0.10 768.08 ± 0.10 763.64 ± 0.10 759.36 ± 0.10 750.46 ± 0.10 825.34 ± 0.40 818.10 ± 0.40 810.87 ± 0.40 803.40 ± 0.40

ρexp − ρcalc kg ⋅ m−3

Ref. (Symbol in Fig. 1)

−0.29 −0.44 −0.60 −0.67 −0.71 −0.40 0.14 −0.51 −0.41 0.09 −0.17 0.00 −0.09 −0.34 −0.20 −0.12 0.04 −0.68 −0.50 0.03 −0.31 −0.34 −0.45 5.72 −0.72 −0.41 0.09 −0.31 −0.28 0.09 −0.11 −0.11 0.55 -0.01 0.21 −0.12 −0.27 0.08 −0.11 −0.07 −0.13 −0.68 −0.61 −0.44 −0.41

76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell1) 76-hal/ell1) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 78-dap/don(✕ ) 78-dap/don1) 78-dap/don1) 78-dap/don1) 78-red/nai-11) 78-red/nai-1(✕ ) 79-dia/tar(∇) 79-dia/tar(∇) 79-dia/tar(∇) 79-dia/tar(∇) 83-dap/del(◆) 83-dap/del(◆) 83-dap/del1) 83-dap/del(◆) 83-dap/del(◆) 84-sak/nak( ) 85-dap/don(✕ ) 85-dap/don(✕ ) 85-dap/don1) 85-dap/don1) 86-rig/mar1) 86-rig/mar1) 86-rig/mar(✕ ) 86-rig/mar(✕ ) 93-gar/ban-1( ) 93-gar/ban-1( ) 93-gar/ban-1( ) 93-gar/ban-1( ) 93-gar/ban-1( ) 93-gar/ban-1( ) 93-gar/ban-1( ) 93-gar/ban-1( ) 93-gar/ban-1( ) 93-gar/ban-1( ) 94-rom/pel(✕ ) 94-rom/pel1) 94-rom/pel1) 94-rom/pel1)

Not included in Fig. 1..

cont. Landolt-Börnstein New Series IV/8G

50

2.1.2 Alkanols, C5 - C6

1-Pentanol (cont.)

ρ

ρ

Further references: [1854-kop, 1864-lan, 1871-lie/ros-3, 1880-bru-1, 1883-sch-3, 1884-zan, 1886-gar, 1892-lan/jah, 1894-jah/mol, 13-kis-3, 13-rom, 23-pop, 24-bou, 24-bus-1, 24-lie, 27-ver/coo, 28-llo/bro, 29-sim, 30-err/she, 30-she, 32-tim/hen, 33-but/tho, 35-but/ram, 39-lar/hun, 45-add, 48-jon/bow, 48-lad/smi, 48-vog-2, 48-wei, 49-tsc/ric, 50-mum/phi, 50-pic/zie, 50-sac/sau, 52-coo, 52-von, 54-dub/luf, 59-ale, 59-lis/kor, 63-hov/sea, 63-tho/mea, 67-gol/per, 68-ano, 70-mye/cle, 73-khi/ale, 73-min/rue, 74-rao/nai, 74-rao/nai-1, 75-mat/fer, 76-kow/kas, 76-red/nai, 78-ast, 78-paz/gar, 78-tre/ben, 79-gyl/apa, 79-kiy/ben, 81-joo/arl, 81-nai/nai, 81-sjo/dyh, 82-kar/red, 82-nai/nai, 82-ort, 82-ven/dha, 83-fuk/ogi, 85-fer/pin, 85-ort/paz-1, 85-sar/paz, 86-ash/sri, 86-ort/paz-1, 86-san/sha, 86-tan/toy, 87-fer/ber, 89-ala/sal, 89-ort/sus, 89-vij/nai, 90-sri/nai, 90-vij/nai, 91-gar/her, 91-ram/muk, 91-yos/kat, 93-ami/ara, 93-ami/rai, 94-kim/lee, 94-kum/nai, 94-kum/nai-1, 94-ven/ven, 94-yu /tsa-1, 95-org/igl, 95-red/ram-1, 96-elb, 98-ami/ban, 98-ami/pat-1, 98-pai/che].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont.

Landolt-Börnstein New Series IV/8G

2.1.2 Alkanols, C5 - C6

51

1-Pentanol (cont.) Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ).

ρ ± σ fit kg ⋅ m−3

T K

875.72 ± 0.34 868.27 ± 0.34 860.92 ± 0.33 853.64 ± 0.33 846.40 ± 0.31 839.17 ± 0.30 831.94 ± 0.28 824.68 ± 0.26 817.35 ± 0.23 815.02 ± 0.23 811.31 ± 0.22 809.93 ± 0.21 802.41 ± 0.20 794.74 ± 0.19

210.00 220.00 230.00 240.00 250.00 260.00 270.00 280.00 290.00 293.15 298.15 300.00 310.00 320.00

ρ ± σ fit kg ⋅ m−3

T K

786.91 ± 0.18 778.88 ± 0.19 770.64 ± 0.20 762.16 ± 0.23 753.41 ± 0.27 744.36 ± 0.32 734.99 ± 0.40 725.27 ± 0.49 715.18 ± 0.60 704.69 ± 0.74 693.77 ± 0.91 682.40 ± 1.10 670.55 ± 1.32 658.20 ± 1.57

330.00 340.00 350.00 360.00 370.00 380.00 390.00 400.00 410.00 420.00 430.00 440.00 450.00 460.00

d-2-Pentanol

[31087-44-2]

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.785. Coefficient ρ = A + BT 1039.28 A B −0.780 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

293.15 298.15 298.15 1)

−3

kg ⋅ m

810.1 ± 1.0 807.9 ± 1.5 816.1 ± 3.0

ρexp − ρcalc

Ref.

kg ⋅ m−3

−0.52 1.18 9.38

43-bra 56-ike/kep 60-ter/kep1)

Not included in calculation of linear coefficients.

Table 3. Recommended values. T K

290.00 293.15 298.15

Landolt-Börnstein New Series IV/8G

ρexp ± 2σ est kg ⋅ m−3

813.1 ± 1.2 810.6 ± 1.1 806.7 ± 1.1

T K

470.00 480.00 490.00 500.00 510.00 520.00 530.00 540.00 550.00 560.00 570.00 580.00

C5H12O

ρ ± σ fit kg ⋅ m−3 645.32 ± 1.86 631.51 ± 1.93 616.78 ± 1.95 601.48 ± 1.97 585.68 ± 1.99 569.16 ± 2.03 551.43 ± 2.09 531.69 ± 2.18 508.81 ± 2.33 481.13 ± 2.62 445.87 ± 3.28 396.14 ± 5.29

MW = 88.15

19

52

2.1.2 Alkanols, C5 - C6

2-Pentanol

[6032-29-7]

C5H12O

MW = 88.15

20

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 5.1481 · 10−1 (combined temperature ranges, weighted), σc,uw = 9.2505 · 10−2 (combined temperature ranges, unweighted). T = 233.15 to 381.35 K ρ = A + BT + CT 2 + DT 3 + … 9.37043 · 102 −5.69541 · 10−2 −1.29071 · 10−3

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 3 −3 − in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 273.15 824.79 ± 0.50 −0.39 32-ell/rei(✕ ) 293.25 806.90 ± 0.50 −2.45 298.15 805.26 ± 0.50 −0.07 32-ell/rei1) 303.25 801.50 ± 0.50 0.42 273.15 824.68 ± 0.50 −0.50 32-tim/hen(✕ ) 314.45 792.30 ± 0.50 0.79 288.15 813.17 ± 0.50 −0.29 32-tim/hen(✕ ) 323.95 783.60 ± 0.60 0.46 303.15 801.18 ± 0.50 0.02 32-tim/hen1) 347.75 761.70 ± 0.60 0.55 298.15 805.25 ± 0.30 −0.08 35-but/ram(◆) 366.65 742.80 ± 0.60 0.15 293.15 808.80 ± 0.40 −0.63 50-pic/zie(✕ ) 381.35 727.40 ± 0.70 −0.22 293.15 809.70 ± 0.30 0.27 52-coo( ) 298.15 805.60 ± 0.30 0.27 293.15 809.80 ± 0.40 0.37 54-pom/foo-1(✕ ) 298.15 805.16 ± 0.30 −0.17 233.15 854.90 ± 1.00 1.30 58-cos/bow(✕ ) 303.15 800.97 ± 0.30 −0.19 253.15 840.20 ± 0.60 0.29 58-cos/bow(✕ ) 308.15 796.97 ± 0.30 0.04 273.15 824.60 ± 0.60 −0.58 58-cos/bow(✕ ) 318.15 788.26 ± 0.30 −0.02 293.15 808.90 ± 0.60 −0.53 58-cos/bow1) 323.15 783.75 ± 0.30 −0.10 313.15 791.90 ± 0.60 −0.74 58-cos/bow1) 298.15 805.50 ± 0.20 0.17 333.15 774.20 ± 0.60 −0.61 58-cos/bow(✕ ) 303.15 801.00 ± 0.20 −0.16 353.15 755.10 ± 0.70 −0.86 58-cos/bow(✕ ) 308.15 796.90 ± 0.20 −0.03 373.15 730.40 ± 0.70 −5.67 58-cos/bow1) 313.15 792.80 ± 0.20 0.16

1)

Ref. (Symbol in Fig. 1) 63-tho/mea1) 63-tho/mea1) 63-tho/mea(✕ ) 63-tho/mea(✕ ) 63-tho/mea(✕ ) 63-tho/mea(✕ ) 63-tho/mea(✕ ) 82-dap/don(∇) 86-ort/paz-1(∆) 86-ort/paz-1(∆) 86-ort/paz-1(∆) 86-ort/paz-1(∆) 86-ort/paz-1(∆) 86-rig/mar( ) 86-rig/mar( ) 86-rig/mar( ) 86-rig/mar( )

Not included in Fig. 1.

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

230.00 240.00 250.00 260.00 270.00 280.00 290.00

ρ ± σ fit kg ⋅ m−3 855.66 ± 1.21 849.03 ± 0.96 842.13 ± 0.75 834.98 ± 0.59 827.57 ± 0.47 819.90 ± 0.40 811.98 ± 0.36

T K

293.15 298.15 300.00 310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 809.43 ± 0.35 805.33 ± 0.34 803.79 ± 0.34 795.35 ± 0.36 786.65 ± 0.40 777.69 ± 0.45 768.47 ± 0.51

T K

350.00 360.00 370.00 380.00 390.00

ρ ± σ fit kg ⋅ m−3 759.00 ± 0.58 749.26 ± 0.66 739.27 ± 0.74 729.02 ± 0.82 718.51 ± 0.89

cont.

Landolt-Börnstein New Series IV/8G

2.1.2 Alkanols, C5 - C6

53

2-Pentanol (cont.)

ρ

ρ

Further references: [1876-lin, 11-pic/ken, 14-vav, 19-eyk, 23-bru, 23-clo/joh, 25-fai, 26-mun, 27-nor/cor, 30-err/she, 36-nor/has, 37-gin/bau, 56-goe/mcc, 63-mcc/lai].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

3-Pentanol

[584-02-1]

C5H12O

MW = 88.15

21

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 1.0029 (combined temperature ranges, weighted), σc,uw = 1.4273 · 10−1 (combined temperature ranges, unweighted). Coefficient A B C

T = 273.15 to 381.35 K ρ = A + BT + CT 2 + DT 3 + … 9.59951 · 102 −9.37135 · 10−2 −1.30516 · 10−3 cont.

Landolt-Börnstein New Series IV/8G

54

2.1.2 Alkanols, C5 - C6

3-Pentanol (cont.) Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

−3

kg ⋅ m

298.15 273.15 288.15 303.15 303.15 293.15 293.15 293.15 298.15

815.40 ± 0.50 836.79 ± 1.00 824.64 ± 1.00 811.78 ± 1.00 812.20 ± 1.00 820.20 ± 0.40 820.30 ± 0.50 820.70 ± 0.40 815.00 ± 0.50

ρexp − ρcalc Ref. (Symbol in Fig. 1) kg ⋅ m−3

−0.59 −0.18 0.06 0.18 0.60 −0.12 −0.02 0.38 −0.99

23-bru( ) 32-tim/hen(✕ ) 32-tim/hen(✕ ) 32-tim/hen(✕ ) 33-nev/jat(✕ ) 50-lad/smi(∆) 50-pic/zie(✕ ) 54-pom/foo-1(∇) 63-mcc/lai(✕ )

T K

292.55 303.05 314.45 323.97 347.75 366.65 381.35 298.15

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

820.80 ± 0.40 811.90 ± 0.40 801.50 ± 0.40 792.80 ± 0.50 769.80 ± 0.50 750.10 ± 0.50 733.60 ± 0.60 815.20 ± 0.30

−0.03 0.21 0.07 0.19 0.27 −0.04 −0.81 −0.79

kg ⋅ m

Ref. (Symbol in Fig. 1) 63-tho/mea(✕ ) 63-tho/mea(✕ ) 63-tho/mea(✕ ) 63-tho/mea(✕ ) 63-tho/mea(✕ ) 63-tho/mea(✕ ) 63-tho/mea(✕ ) 82-dap/don( )

ρ

ρ

Further references: [1875-wag/say, 13-pic/ken, 14-vav, 19-eyk, 27-nor/cor, 30-err/she, 35-les/lom, 36-spe, 37-gin/bau, 37-she/mat, 40-whi/sur, 48-wei, 52-coo, 53-ano-1, 56-goe/mcc, 56-shu/bel].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont. Landolt-Börnstein New Series IV/8G

2.1.2 Alkanols, C5 - C6

55

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ).

ρ ± σ fit kg ⋅ m−3

T K

T K

839.50 ± 1.12 831.39 ± 0.82 823.01 ± 0.62 820.32 ± 0.57 815.99 ± 0.52

270.00 280.00 290.00 293.15 298.15

300.00 310.00 320.00 330.00 340.00

2,2-Dimethyl-1-butanol

ρ ± σ fit kg ⋅ m−3 814.37 ± 0.51 805.47 ± 0.48 796.31 ± 0.50 786.89 ± 0.54 777.21 ± 0.57

[1185-33-7]

ρ ± σ fit kg ⋅ m−3

T K

767.27 ± 0.60 757.07 ± 0.62 746.60 ± 0.65 735.87 ± 0.68 724.89 ± 0.74

350.00 360.00 370.00 380.00 390.00

C6H14O

MW = 102.18

22

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 3.0286 · 10−1 (combined temperature ranges, weighted), σc,uw = 9.4262 · 10−2 (combined temperature ranges, unweighted). T = 278.15 to 408.15 K ρ = A + BT + CT 2 + DT 3 + …

Coefficient A B C

9.76530 · 102 −2.16929 · 10−1 −9.82641 · 10−4

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 278.15 288.15 298.15 308.15 318.15 328.15 338.15 348.15 358.15

ρexp ± 2σ est

ρexp − ρcalc kg ⋅ m−3

Ref. (Symbol in Fig. 1)

0.84 −0.06 −0.23 −0.18 −0.15 −0.06 0.16 0.13 0.23

40-hov/lan-2( 40-hov/lan-2( 40-hov/lan-2( 40-hov/lan-2( 40-hov/lan-2( 40-hov/lan-2( 40-hov/lan-2( 40-hov/lan-2( 40-hov/lan-2(

−3

kg ⋅ m

841.01 ± 0.40 832.37 ± 0.40 824.27 ± 0.40 816.20 ± 0.40 807.90 ± 0.40 799.47 ± 0.40 790.97 ± 0.40 782.03 ± 0.40 773.02 ± 0.40

) ) ) ) ) ) ) ) )

T K 368.15 378.15 388.15 398.15 408.15 293.15 293.15 293.15

ρexp ± 2σ est

ρexp − ρcalc kg ⋅ m−3

Ref. (Symbol in Fig. 1)

0.37 0.32 0.10 −0.01 −0.28 −0.19 −0.99 0.01

40-hov/lan-2( 40-hov/lan-2( 40-hov/lan-2( 40-hov/lan-2( 40-hov/lan-2( 50-pic/zie( ) 64-blo/hag(∆) 65-shu/puz(∇)

−3

kg ⋅ m

763.86 ± 0.40 754.30 ± 0.40 744.38 ± 0.40 734.38 ± 0.40 724.02 ± 0.40 828.30 ± 0.60 827.50 ± 1.00 828.50 ± 1.00

) ) ) ) )

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K 270.00 280.00 290.00 293.15 298.15 300.00

ρ ± σ fit kg ⋅ m−3 846.32 ± 0.76 838.75 ± 0.68 830.98 ± 0.61 828.49 ± 0.59 824.50 ± 0.56 823.01 ± 0.56

T K 310.00 320.00 330.00 340.00 350.00 360.00

ρ ± σ fit kg ⋅ m−3 814.85 ± 0.52 806.49 ± 0.49 797.93 ± 0.46 789.18 ± 0.45 780.23 ± 0.43 771.09 ± 0.41

T K 370.00 380.00 390.00 400.00 410.00 420.00

ρ ± σ fit kg ⋅ m−3 761.74 ± 0.40 752.20 ± 0.40 742.47 ± 0.41 732.54 ± 0.44 722.41 ± 0.50 712.08 ± 0.57

cont.

Landolt-Börnstein New Series IV/8G

56

2.1.2 Alkanols, C5 - C6

2,2-Dimethyl-1-butanol (cont.)

ρ

ρ

Further references: [04-bou/bla-2, 38-gin/web].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

2,3-Dimethyl-1-butanol

[19550-30-2]

C6H14O

MW = 102.18

23

Table 1. Experimental and recommended values with uncertainties. T K 298.15 293.65 298.15 1)

ρexp ± 2σ est

T K 293.15 293.15 293.15

Ref.

−3

kg ⋅ m

823.7 ± 2.0 829.7 ± 0.6 823.0 ± 2.0

59-tsu/hay1) 13-gor 35-lev/mar1)

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

830.1 ± 0.6 830.6 ± 1.0 830.0 ± 0.6

50-pic/zie 52-coo Recommended

Not included in calculation of recommended value.

(R)-2,3-Dimethyl-1-butanol

[15019-27-9]

C6H14O

MW = 102.18

24

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

823.7 ± 0.8

59-tsu/hay

Landolt-Börnstein New Series IV/8G

2.1.2 Alkanols, C5 - C6 2,3-Dimethyl-2-butanol

[594-60-5]

57 C6H14O

MW = 102.18

25

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 6.3478 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.4692 · 10−1 (combined temperature ranges, unweighted). T = 273.15 to 388.15 K ρ = A + BT + CT 2 + DT 3 + … 9.39911 · 102 6.32414 · 10−2 −1.58086 · 10−3

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 273.15 292.15 278.15 288.15 298.15 308.15 318.15 328.15 338.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

838.60 ± 1.00 821.90 ± 1.00 835.11 ± 0.20 826.76 ± 0.20 818.59 ± 0.20 809.51 ± 0.20 799.84 ± 0.20 790.56 ± 0.20 780.70 ± 0.20

−0.64 −1.56 −0.08 −0.11 0.35 0.22 −0.18 0.13 0.17

Ref. (Symbol in Fig. 1) 1879-pav(∇) 1879-pav(∇) 41-hov/lan( 41-hov/lan( 41-hov/lan( 41-hov/lan( 41-hov/lan( 41-hov/lan( 41-hov/lan(

) ) ) ) ) ) )

T K 348.15 358.15 368.15 378.15 388.15 293.15 298.15 293.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

770.02 ± 0.20 759.67 ± 0.20 748.92 ± 0.20 738.04 ± 0.20 726.36 ± 0.20 823.60 ± 0.40 819.30 ± 0.40 822.30 ± 0.60

−0.29 −0.11 −0.01 0.27 0.07 1.00 1.06 −0.30

Ref. (Symbol in Fig. 1)

41-hov/lan( ) 41-hov/lan( ) 41-hov/lan( ) 41-hov/lan( ) 41-hov/lan( ) 47-how/mea( ) 47-how/mea( ) 50-pic/zie(∆)

Further references: [1873-fri/sil, 52-lev/tan, 52-ove/ber].

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15 300.00

ρ ± σ fit kg ⋅ m−3 841.74 ± 0.73 833.68 ± 0.60 825.30 ± 0.48 822.60 ± 0.45 818.24 ± 0.40 816.61 ± 0.38

T K

310.00 320.00 330.00 340.00 350.00 360.00

ρ ± σ fit kg ⋅ m−3 807.60 ± 0.31 798.27 ± 0.25 788.62 ± 0.21 778.67 ± 0.18 768.39 ± 0.17 757.80 ± 0.17

T K

370.00 380.00 390.00 400.00

ρ ± σ fit kg ⋅ m−3 746.89 ± 0.19 735.67 ± 0.24 724.13 ± 0.31 712.27 ± 0.40

cont.

Landolt-Börnstein New Series IV/8G

58

2.1.2 Alkanols, C5 - C6

ρ

ρ

2,3-Dimethyl-2-butanol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

3,3-Dimethyl-1-butanol

[624-95-3]

C6H14O

MW = 102.18

26

C6H14O

MW = 102.18

27

Table 1. Experimental values with uncertainties. T K

297.15 288.15 298.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

814.0 ± 2.0 844.0 ± 10.0 809.7 ± 2.0

41-hus/age 49-mal/vol 56-sar/new

3,3-Dimethyl-2-butanol

[464-07-3]

Table 1. Experimental and recommended values with uncertainties. T K

293.15 298.15 298.15 293.15 1)

ρexp ± 2σ est

Ref.

kg ⋅ m−3

818.5 ± 1.0 810.0 ± 3.0 815.7 ± 2.0 818.4 ± 1.0

14-low 33-ste1) 38-gin/web1) 50-mos/lac

T K

298.15 293.15 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

812.2 ± 2.0 816.7 ± 1.0 817.9 ± 1.2

56-sar/new1) 50-pic/zie Recommended

Not included in calculation of recommended value. Landolt-Börnstein New Series IV/8G

2.1.2 Alkanols, C5 - C6 (S)-3,3-Dimethyl-2-butanol

[1517-67-5]

59 C6H14O

MW = 102.18

28

C6H14O

MW = 102.18

29

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

810.0 ± 2.0

33-ste

2-Ethyl-1-butanol

[97-95-0]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 2.6167 · 10−1 (combined temperature ranges, weighted), σc,uw = 5.9806 · 10−2 (combined temperature ranges, unweighted). T = 288.15 to 418.15 K ρ = A + BT + CT 2 + DT 3 + … 9.36526 · 102 1.79278 · 10−2 −1.26674 · 10−3

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

293.15 293.15 278.15 288.15 298.15 308.15 318.15 328.15 338.15 348.15 358.15 1)

ρexp ± 2σ est −3

kg ⋅ m

832.60 ± 1.00 832.80 ± 0.50 845.04 ± 0.50 837.33 ± 0.50 829.53 ± 0.50 822.03 ± 0.50 814.11 ± 0.50 805.93 ± 0.50 797.38 ± 0.50 789.18 ± 0.50 780.51 ± 0.50

ρexp − ρcalc kg ⋅ m−3

−0.32 −0.12 1.53 0.82 0.26 0.27 0.10 −0.07 −0.36 −0.05 0.05

Ref. (Symbol in Fig. 1) 38-whi/kar(✕ ) 39-gol/tay(◆) 40-hov/lan-21) 40-hov/lan-2(∆) 40-hov/lan-2(∆) 40-hov/lan-2(∆) 40-hov/lan-2(∆) 40-hov/lan-2(∆) 40-hov/lan-2(∆) 40-hov/lan-2(∆) 40-hov/lan-2(∆)

T K

368.15 378.15 388.15 398.15 408.15 418.15 293.15 293.15 298.15 298.15

ρexp ± 2σ est

ρexp − ρcalc kg ⋅ m−3

−3

kg ⋅ m

771.39 ± 0.50 762.31 ± 0.50 752.47 ± 0.50 742.87 ± 0.50 732.74 ± 0.50 722.29 ± 0.50 833.10 ± 0.60 832.90 ± 0.50 829.11 ± 0.20 829.07 ± 0.20

−0.05 0.15 −0.17 0.01 −0.08 −0.24 0.18 −0.02 −0.16 −0.20

Ref. (Symbol in Fig. 1) 40-hov/lan-2(∆) 40-hov/lan-2(∆) 40-hov/lan-2(∆) 40-hov/lan-2(∆) 40-hov/lan-2(∆) 40-hov/lan-2(∆) 52-coo(✕ ) 68-ano(∇) 84-kim/ben( ) 85-ort/paz-2( )

Not included in Fig. 1.

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

280.00 290.00 293.15 298.15 300.00 310.00

ρ ± σ fit kg ⋅ m−3 842.23 ± 0.55 835.19 ± 0.52 832.92 ± 0.52 829.27 ± 0.51 827.90 ± 0.51 820.35 ± 0.51

T K

320.00 330.00 340.00 350.00 360.00 370.00

ρ ± σ fit kg ⋅ m−3 812.55 ± 0.51 804.49 ± 0.52 796.19 ± 0.52 787.62 ± 0.52 778.81 ± 0.52 769.74 ± 0.52

T K

380.00 390.00 400.00 410.00 420.00 430.00

ρ ± σ fit kg ⋅ m−3 760.42 ± 0.51 750.85 ± 0.51 741.02 ± 0.52 730.94 ± 0.55 720.60 ± 0.60 710.01 ± 0.68 cont.

Landolt-Börnstein New Series IV/8G

60

2.1.2 Alkanols, C5 - C6

2-Ethyl-1-butanol (cont.)

ρ

ρ

Further references: [48-wei, 50-pic/zie, 53-ano-1, 58-ano-5, 58-cos/bow].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

1-Hexanol

[111-27-3]

C6H14O

MW = 102.18

30

Tc = 611.00 K [89-tej/lee] ρc = 268.00 kg·m−3 [89-tej/lee] Table 1. Coefficients for the polynomial expansion equations. Standard deviations (see introduction): σ = 7.2858 · 10−1 (low temperature range), σc,w = (4.6480 · 10−1 combined temperature ranges, weighted), σc,uw = 2.7537 · 10−1 (combined temperature ranges, unweighted).

Coefficient

A B C D

T = 235.72 to 500.00 K ρ = A + BT + CT 2 + DT 3 + …

1.01544 · 103 −7.78875 · 10−1 8.80075 · 10−4 −1.73223 · 10−6

T = 500.00 to 611.00 K ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)] [ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] 8.35316 · 10−1 −1.13272 · 10−2 8.40546 · 10−5 −2.64908 · 10−7 cont.

Landolt-Börnstein New Series IV/8G

2.1.2 Alkanols, C5 - C6

61

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 273.15 298.15 278.15 288.15 298.15 308.15 318.15 328.15 338.15 348.15 358.15 368.15 378.15 388.15 398.15 408.15 418.15 432.15 253.15 273.15 293.15 313.15 333.15 353.15 373.15 393.15 413.15 433.15 453.15 473.15 493.15 513.15 273.15 273.15 293.15 313.15 333.15 353.15 373.15 393.15 413.15 433.15 453.15 473.15 493.15 513.15 533.15 1)

ρexp ± 2σ est −3

kg ⋅ m

833.34 ± 0.20 815.79 ± 0.20 829.83 ± 0.50 822.67 ± 0.50 815.54 ± 0.50 808.34 ± 0.50 801.03 ± 0.50 793.56 ± 0.50 785.34 ± 0.50 778.20 ± 0.50 770.22 ± 0.50 762.12 ± 0.50 753.39 ± 0.60 744.60 ± 0.60 735.48 ± 0.60 726.02 ± 0.60 716.16 ± 0.60 702.09 ± 0.60 850.30 ± 1.00 835.90 ± 1.00 821.70 ± 1.00 807.00 ± 1.00 792.40 ± 1.00 776.60 ± 1.00 759.90 ± 1.00 743.20 ± 1.00 724.70 ± 1.00 705.60 ± 1.50 685.00 ± 1.50 663.80 ± 1.50 640.60 ± 1.50 616.30 ± 1.50 832.82 ± 0.10 834.00 ± 1.50 819.00 ± 1.50 804.00 ± 1.50 788.00 ± 1.50 773.00 ± 1.50 757.00 ± 1.50 739.00 ± 1.50 720.00 ± 1.50 700.00 ± 1.50 679.00 ± 1.50 657.00 ± 1.50 634.00 ± 1.50 610.00 ± 1.50 580.00 ± 1.50

Not included in Fig. 1.

Landolt-Börnstein New Series IV/8G

ρexp − ρcalc kg ⋅ m

Ref. (Symbol in Fig. 1)

0.29 0.25 0.23 0.04 0.00 0.03 0.09 0.15 −0.37 0.35 0.43 0.58 0.31 0.19 −0.03 −0.35 −0.82 −1.31 3.74 2.85 2.60 2.36 2.82 2.76 2.56 3.21 2.99 3.19 2.98 3.35 2.98 3.97 −0.23 0.95 −0.10 −0.64 −1.58 −0.84 −0.34 −0.99 −1.71 −2.41 −3.02 −3.45 −3.62 −2.33 −1.60

32-ell/rei(✕ ) 32-ell/rei1) 38-hov/lan1) 38-hov/lan1) 38-hov/lan1) 38-hov/lan1) 38-hov/lan1) 38-hov/lan1) 38-hov/lan1) 38-hov/lan1) 38-hov/lan1) 38-hov/lan1) 38-hov/lan(✕ ) 38-hov/lan(✕ ) 38-hov/lan(✕ ) 38-hov/lan(✕ ) 38-hov/lan(✕ ) 38-hov/lan(✕ ) 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 59-mck/ski(∆) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ )

−3

T K 553.15 563.15 573.15 583.15 588.15 593.15 598.15 603.15 605.15 607.15 235.72 249.28 262.88 273.00 286.10 293.12 293.14 303.16 313.13 323.08 333.14 303.15 293.15 298.15 303.15 308.15 303.15 313.15 290.10 305.90 350.80 380.90 422.80 283.15 298.15 308.15 323.15 323.15 328.15 333.15 338.15 343.15 348.15 353.15 358.15 363.15 373.15

ρexp ± 2σ est −3

kg ⋅ m

ρexp − ρcalc kg ⋅ m−3

545.00 ± 1.50 −0.12 0.10 524.00 ± 1.50 0.24 500.00 ± 1.50 1.53 473.00 ± 2.00 1.89 457.00 ± 2.00 436.00 ± 2.00 −0.66 410.00 ± 3.00 −5.23 385.00 ± 5.00 −3.80 370.00 ± 5.00 −5.74 347.00 ± 5.00 −12.95 1.19 859.24 ± 0.16 0.45 849.58 ± 0.16 840.02 ± 0.16 −0.02 832.97 ± 0.16 −0.18 823.72 ± 0.16 −0.35 818.88 ± 0.16 −0.24 818.80 ± 0.16 −0.31 811.63 ± 0.16 −0.30 804.42 ± 0.16 −0.24 797.04 ± 0.16 −0.20 789.42 ± 0.16 −0.17 0.01 811.95 ± 0.04 818.75 ± 0.10 −0.35 815.34 ± 0.10 −0.20 811.62 ± 0.10 −0.32 808.02 ± 0.10 −0.29 811.94 ± 0.10 −0.00 804.48 ± 0.10 −0.16 820.00 ± 0.82 −1.26 807.50 ± 0.81 −2.45 743.40 ± 0.74 −32.33 744.00 ± 0.74 −6.72 712.30 ± 0.71 −0.23 822.14 ± 0.15 −3.99 815.12 ± 0.15 −0.42 807.93 ± 0.15 −0.38 796.86 ± 0.15 −0.33 0.15 797.34 ± 0.10 0.68 794.09 ± 0.10 0.09 789.67 ± 0.10 0.31 786.02 ± 0.10 781.78 ± 0.10 −0.02 777.68 ± 0.10 −0.17 0.05 773.89 ± 0.10 769.75 ± 0.10 −0.04 765.47 ± 0.10 −0.22 757.03 ± 0.10 −0.31

Ref. (Symbol in Fig. 1) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr1) 73-fin(✕ ) 73-fin(✕ ) 73-fin(✕ ) 73-fin(✕ ) 73-fin(✕ ) 73-fin1) 73-fin1) 73-fin1) 73-fin1) 73-fin1) 73-fin(✕ ) 74-rao/nai-1( ) 78-jel/leo(◆) 78-jel/leo1) 78-jel/leo(◆) 78-jel/leo(◆) 78-red/nai-1(∇) 78-red/nai-1(∇) 79-gyl/apa1) 79-gyl/apa1) 79-gyl/apa1) 79-gyl/apa1) 79-gyl/apa(✕ ) 86-hei/sch(✕ ) 86-hei/sch1) 86-hei/sch1) 86-hei/sch(✕ ) 93-gar/ban-1( ) 93-gar/ban-1( ) 93-gar/ban-1( ) 93-gar/ban-1( ) 93-gar/ban-1( ) 93-gar/ban-1( ) 93-gar/ban-1( ) 93-gar/ban-1( ) 93-gar/ban-1( ) 93-gar/ban-1( )

cont.

62

2.1.2 Alkanols, C5 - C6

1-Hexanol (cont.)

ρ

ρ

Further references: [1877-lie/jan, 1883-fre, 1884-zan, 1886-gar, 18-bro/hum, 19-beh, 27-nor/cor, 27-ver/coo, 29-kel-3, 29-mah/das, 30-wal/ros, 33-but/tho, 35-bil/gis, 35-but/ram, 39-gol/tay, 41-hus/age, 45-add, 48-jon/bow, 48-lad/smi, 48-vog-2, 48-wei, 50-gor, 50-mum/phi, 50-pic/zie, 50-sac/sau, 52-coo, 52-eri-1, 53-ano-1, 53-par/cha, 54-naz/kak-2, 56-shu/bel, 57-col/fal, 58-ano-5, 58-lin/tua, 62-bro/smi, 63-nik, 68-ano, 68-pfl/pop, 68-rao/chi, 69-kat/pat, 70-mye/cle, 70-puz/bul, 74-moo/wel, 74-rao/nai, 75-hsu/cle, 75-mat/fer, 76-kow/kas, 76-red/nai, 78-ast, 78-dap/don, 78-paz/gar, 78-tre/ben, 79-dia/tar, 79-kiy/ben, 80-tre/ben, 81-han/hal, 81-kim/ben, 81-kor/kov, 81-nai/nai, 81-sjo/dyh, 82-nai/nai, 82-ort, 82-sin/sin, 82-ven/dha, 83-fuk/ogi, 83-kim/ben, 84-bra/pin, 84-ort/ang, 84-sak/nak, 85-fer/pin, 85-ort, 85-ort/paz-1, 85-sar/paz, 85-sin/sin, 85-sin/sin-1, 86-ash/sri, 86-dew/meh, 86-sin/sin, 86-tan/toy, 86-wag/hei, 87-dew/meh, 88-ort/gar, 89-ala/sal, 89-dew/gup, 89-mat/mak-1, 89-sin/sin, 89-vij/nai, 90-vij/nai, 91-fen/wan, 91-ram/muk, 92-lie/sen-1, 93-ami/ara, 93-ami/rai, 93-yan/mae, 94-kim/lee, 94-kum/nai, 94-kum/nai-1, 94-ven/ven, 94-yu /tsa, 94-yu /tsa-1, 95-fra/jim, 95-fra/men, 96-elb, 98-ami/ban, 98-ami/pat-1].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont. Landolt-Börnstein New Series IV/8G

2.1.2 Alkanols, C5 - C6

63

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ).

ρ ± σ fit kg ⋅ m−3

T K

861.78 ± 0.51 855.25 ± 0.37 848.66 ± 0.25 841.98 ± 0.16 835.20 ± 0.14 828.32 ± 0.13 821.33 ± 0.10 819.10 ± 0.10 815.54 ± 0.10 814.21 ± 0.10 806.96 ± 0.10 799.56 ± 0.12 792.00 ± 0.12 784.27 ± 0.15

230.00 240.00 250.00 260.00 270.00 280.00 290.00 293.15 298.15 300.00 310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3

T K

350.00 360.00 370.00 380.00 390.00 400.00 410.00 420.00 430.00 440.00 450.00 460.00 470.00 480.00

2-Hexanol

776.37 ± 0.21 768.28 ± 0.29 759.99 ± 0.38 751.50 ± 0.47 742.78 ± 0.57 733.84 ± 0.68 724.65 ± 0.79 715.22 ± 0.90 705.52 ± 1.01 695.56 ± 1.12 685.31 ± 1.23 674.77 ± 1.34 663.93 ± 1.45 652.78 ± 1.55 [626-93-7]

ρ ± σ fit kg ⋅ m−3

T K

490.00 500.00 510.00 520.00 530.00 540.00 550.00 560.00 570.00 580.00 590.00 600.00 610.00

C6H14O

641.30 ± 1.64 629.49 ± 1.73 616.68 ± 2.28 602.39 ± 2.29 586.79 ± 2.28 569.84 ± 2.27 551.33 ± 2.26 530.85 ± 2.27 507.74 ± 2.32 480.94 ± 2.44 448.56 ± 2.72 406.21 ± 3.58 324.59 ± 9.90

MW = 102.18

31

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 4.6999 · 10−1 (combined temperature ranges, weighted), σc,uw = 8.6236 · 10−2 (combined temperature ranges, unweighted). T = 273.15 to 413.15 K ρ = A + BT + CT 2 + DT 3 + … 9.26903 · 102 −3.13386 · 10−3 −1.30510 · 10−3

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

273.15 293.15 293.15 371.65 393.15 273.15 288.15 298.15 298.15 278.15 288.15 1)

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

828.70 ± 0.60 814.10 ± 0.60 815.00 ± 0.60 744.40 ± 1.00 726.30 ± 1.00 828.30 ± 0.50 817.10 ± 0.50 809.75 ± 0.20 810.80 ± 0.50 825.80 ± 0.50 818.12 ± 0.50

0.03 0.27 1.17 −1.07 2.35 −0.37 −0.54 −0.20 0.85 0.74 0.48

kg ⋅ m

Ref. (Symbol in Fig. 1) 08-zel/prz(✕ ) 08-zel/prz(✕ ) 11-pic/ken(✕ ) 12-pic/ken(✕ ) 12-pic/ken1) 26-van(✕ ) 26-van(✕ ) 32-ell/rei( ) 38-gin/web(◆) 38-hov/lan(✕ ) 38-hov/lan(✕ )

T K

298.15 308.15 318.15 328.15 338.15 348.15 358.15 368.15 378.15 388.15 398.15

ρexp ± 2σ est

ρexp − ρcalc

−3

kg ⋅ m

Ref. (Symbol in Fig. 1)

810.34 ± 0.50 802.21 ± 0.50 794.01 ± 0.50 785.49 ± 0.50 776.74 ± 0.50 767.76 ± 0.50 758.01 ± 0.50 749.26 ± 0.50 738.95 ± 0.60 728.80 ± 0.60 718.43 ± 0.60

0.39 0.20 0.20 0.15 0.13 0.14 -0.36 0.40 −0.14 −0.26 −0.34

38-hov/lan(✕ ) 38-hov/lan(✕ ) 38-hov/lan(✕ ) 38-hov/lan(✕ ) 38-hov/lan(✕ ) 38-hov/lan(✕ ) 38-hov/lan(✕ ) 38-hov/lan(✕ ) 38-hov/lan(✕ ) 38-hov/lan(✕ ) 38-hov/lan(✕ )

kg ⋅ m

−3

Not included in Fig. 1

cont.

Landolt-Börnstein New Series IV/8G

64

2.1.2 Alkanols, C5 - C6

2-Hexanol (cont.)

Table 2. (cont.) ρexp ± 2σ est

T K

kg ⋅ m

Ref. (Symbol in Fig. 1)

707.72 ± 0.60 702.22 ± 0.60 815.00 ± 0.60 814.20 ± 0.60 814.30 ± 0.50 813.56 ± 0.50 809.61 ± 0.50

−0.49 −0.62 1.17 0.37 0.47 −0.27 −0.34

38-hov/lan(✕ ) 38-hov/lan(✕ ) 42-air/bal(✕ ) 50-pic/zie(✕ ) 52-coo(∇) 85-ort(✕ ) 85-ort(✕ )

kg ⋅ m

408.15 413.15 293.15 293.15 293.15 293.15 298.15

ρexp − ρcalc

−3

−3

T K

300.15 302.15 304.15 306.15 308.15 298.15 298.15

ρexp ± 2σ est

ρexp − ρcalc

−3

kg ⋅ m

Ref. (Symbol in Fig. 1)

808.05 ± 0.50 806.46 ± 0.50 804.85 ± 0.50 803.27 ± 0.50 801.89 ± 0.50 809.69 ± 0.10 809.61 ± 0.50

−0.34 −0.35 −0.37 −0.35 −0.12 −0.26 −0.34

85-ort(✕ ) 85-ort(✕ ) 85-ort(✕ ) 85-ort(✕ ) 85-ort(✕ ) 86-ort/paz( ) 94-tar/jun(∆)

kg ⋅ m

−3

ρ

ρ

Further references: [23-clo/joh, 27-nor/cor, 35-les/lom, 39-bar/atk].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont.

Landolt-Börnstein New Series IV/8G

2.1.2 Alkanols, C5 - C6

65

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ).

ρ ± σ fit kg ⋅ m−3

T K

830.92 ± 0.52 823.71 ± 0.50 816.24 ± 0.49 813.83 ± 0.50 809.95 ± 0.50 808.50 ± 0.50

270.00 280.00 290.00 293.15 298.15 300.00

ρ ± σ fit kg ⋅ m−3

T K

800.51 ± 0.52 792.26 ± 0.53 783.74 ± 0.55 774.97 ± 0.57 765.93 ± 0.58 756.63 ± 0.59

310.00 320.00 330.00 340.00 350.00 360.00

(RS)-2-Hexanol

T K

[20281-86-1]

370.00 380.00 390.00 400.00 410.00 420.00

ρ ± σ fit kg ⋅ m−3 747.08 ± 0.60 737.26 ± 0.61 727.18 ± 0.62 716.83 ± 0.65 706.23 ± 0.68 695.37 ± 0.74

C6H14O

MW = 102.18

32

C6H14O

MW = 102.18

33

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 298.15 88-tan/luo 810.0 ± 0.2 3-Hexanol

[623-37-0]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 3.6198 · 10−1 (combined temperature ranges, weighted), σc,uw = 7.2518 · 10−2 (combined temperature ranges, unweighted). T = 273.15 to 409.15 K ρ = A + BT + CT 2 + DT 3 + …

Coefficient A B C

9.66285 · 102 −1.77415 · 10−1 −1.11253 · 10−3

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 273.15 293.15 273.15 293.15 273.15 293.15 298.15 278.15 288.15 298.15 308.15 318.15 328.15 1)

ρexp ± 2σ est −3

kg ⋅ m

833.50 ± 1.00 818.80 ± 1.00 833.50 ± 1.00 818.80 ± 1.00 834.31 ± 1.00 818.23 ± 1.00 814.30 ± 0.50 830.96 ± 0.50 822.73 ± 0.50 814.26 ± 0.50 805.80 ± 0.50 796.97 ± 0.50 788.10 ± 0.50

ρexp − ρcalc −3

kg ⋅ m

−1.32 0.13 −1.32 0.13 −0.51 −0.44 −0.19 0.10 −0.06 −0.23 −0.17 −0.26 −0.17

T K 1875-lie1) 338.15 1875-lie(✕ ) 348.15 1875-lie/vol1) 358.15 1875-lie/vol(✕ ) 368.15 378.15 1876-dec(∇) 388.15 1876-dec(∇) 398.15 38-gin/web(∆) 38-hov/lan( ) 409.15 38-hov/lan( ) 293.15 38-hov/lan( ) 293.15 38-hov/lan( ) 293.15 38-hov/lan( ) 293.15 38-hov/lan( )

Ref. (Symbol in Fig. 1)

ρexp ± 2σ est −3

kg ⋅ m

779.06 ± 0.50 769.72 ± 0.50 759.69 ± 0.50 750.40 ± 0.50 740.13 ± 0.50 730.34 ± 0.50 719.18 ± 0.50 707.06 ± 0.50 819.30 ± 1.00 819.50 ± 1.00 818.60 ± 0.50 819.00 ± 1.00

ρexp − ρcalc kg ⋅ m

Ref. (Symbol in Fig. 1)

−0.02 0.05 −0.35 0.22 0.02 0.53 −0.11 −0.39 0.63 0.83 −0.07 0.33

38-hov/lan( ) 38-hov/lan( ) 38-hov/lan( ) 38-hov/lan( ) 38-hov/lan( ) 38-hov/lan( ) 38-hov/lan( ) 38-hov/lan( ) 42-air/bal(◆) 44-hen/mat(✕ ) 50-pic/zie( ) 52-coo(✕ )

−3

Not included in Fig. 1.

cont. Landolt-Börnstein New Series IV/8G

66

2.1.2 Alkanols, C5 - C6

3-Hexanol (cont.)

ρ

ρ

Further references: [13-pic/ken, 34-les/lom, 35-les/lom, 39-spi/tin-1, 54-naz/kak-3, 56-shu/bel].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15 300.00

ρ ± σ fit kg ⋅ m−3 837.28 ± 0.98 829.39 ± 0.87 821.27 ± 0.78 818.67 ± 0.75 814.49 ± 0.72 812.93 ± 0.71

T K

310.00 320.00 330.00 340.00 350.00 360.00

ρ ± σ fit kg ⋅ m−3 804.37 ± 0.65 795.59 ± 0.61 786.58 ± 0.57 777.36 ± 0.55 767.91 ± 0.52 758.23 ± 0.51

T K

370.00 380.00 390.00 400.00 410.00 420.00

ρ ± σ fit kg ⋅ m−3 748.34 ± 0.50 738.22 ± 0.50 727.88 ± 0.52 717.31 ± 0.56 706.53 ± 0.64 695.52 ± 0.73

Landolt-Börnstein New Series IV/8G

2.1.2 Alkanols, C5 - C6 2-Methyl-1-pentanol

[105-30-6]

67 C6H14O

MW = 102.18

34

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 3.6425 · 10−1 (combined temperature ranges, weighted), σc,uw = 7.9675 · 10−2 (combined temperature ranges, unweighted). T = 273.15 to 408.15 K ρ = A + BT + CT 2 + DT 3 + … 9.25662 · 102 1.79466 · 10−2 −1.24362 · 10−3

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 273.15 273.15 290.75 296.85 278.15 288.15 298.15 308.15 318.15 328.15 1)

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

839.50 ± 1.50 837.40 ± 1.50 824.60 ± 1.50 821.40 ± 1.50 834.70 ± 0.50 827.99 ± 0.50 820.63 ± 0.50 813.07 ± 0.50 805.48 ± 0.50 797.55 ± 0.50

1.72 −0.38 −1.15 −0.00 0.26 0.42 0.17 −0.03 −0.01 −0.08

T K 1883-lie/zei1) 338.15 1883-lie/zei(∇) 348.15 1883-lie/zei(∇) 358.15 1883-lie/zei(∇) 368.15 378.15 38-hov/lan(∆) 388.15 38-hov/lan(∆) 398.15 38-hov/lan(∆) 408.15 38-hov/lan(∆) 293.15 38-hov/lan(∆) 293.15 38-hov/lan(∆)

Ref. (Symbol in Fig. 1)

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

789.50 ± 0.50 781.19 ± 0.50 772.69 ± 0.50 764.13 ± 0.50 754.77 ± 0.50 745.34 ± 0.50 735.69 ± 0.50 725.74 ± 0.50 824.30 ± 0.50 824.00 ± 0.50

−0.03 0.02 0.12 0.41 0.16 0.08 0.03 −0.08 0.25 −0.05

Ref. (Symbol in Fig. 1) 38-hov/lan(∆) 38-hov/lan(∆) 38-hov/lan(∆) 38-hov/lan(∆) 38-hov/lan(∆) 38-hov/lan(∆) 38-hov/lan(∆) 38-hov/lan(∆) 50-pic/zie( ) 68-ano( )

Not included in Fig. 1.

Further references: [24-ter, 27-nor/cor, 36-oli, 51-hau, 52-coo, 53-ano-1, 56-ano-1, 84-bra/pin, 85-ort, 94-tar/jun].

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15 300.00

ρ ± σ fit kg ⋅ m−3 839.85 ± 1.24 833.19 ± 1.01 826.28 ± 0.82 824.05 ± 0.78 820.46 ± 0.71 819.12 ± 0.69

T K

310.00 320.00 330.00 340.00 350.00 360.00

ρ ± σ fit kg ⋅ m−3 811.71 ± 0.60 804.06 ± 0.55 796.15 ± 0.52 788.00 ± 0.51 779.60 ± 0.51 770.95 ± 0.52

T K

370.00 380.00 390.00 400.00 410.00 420.00

ρ ± σ fit kg ⋅ m−3 762.05 ± 0.53 752.90 ± 0.54 743.51 ± 0.55 733.86 ± 0.56 723.97 ± 0.59 713.82 ± 0.63

cont.

Landolt-Börnstein New Series IV/8G

68

2.1.2 Alkanols, C5 - C6

ρ

ρ

2-Methyl-1-pentanol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

2-Methyl-2-pentanol

[590-36-3]

C6H14O

MW = 102.18

35

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 2.6940 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.0135 · 10−1 (combined temperature ranges, unweighted). Coefficient A B C

T = 278.15 to 358.15 K ρ = A + BT + CT 2 + DT 3 + … 9.36813 · 102 −1.65836 · 10−2 −1.37719 · 10−3

cont. Landolt-Börnstein New Series IV/8G

2.1.2 Alkanols, C5 - C6

69

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

−3

kg ⋅ m

826.00 ± 0.50 817.10 ± 0.50 809.68 ± 0.50 801.10 ± 0.50 792.33 ± 0.50

0.35 −0.59 0.23 0.17 0.19

kg ⋅ m

278.15 288.15 298.15 308.15 318.15

ρexp − ρcalc

−3

Ref. (Symbol in Fig. 1)

) ) ) ) )

33-hov/lan( 33-hov/lan( 33-hov/lan( 33-hov/lan( 33-hov/lan(

T K

328.15 338.15 348.15 358.15 293.15

ρexp ± 2σ est

ρexp − ρcalc kg ⋅ m−3

−3

kg ⋅ m

783.02 ± 0.50 773.72 ± 0.50 764.32 ± 0.50 754.11 ± 0.50 813.40 ± 1.00

−0.05 −0.01 0.21 −0.11 −0.20

Ref. (Symbol in Fig. 1)

) ) ) ) )

33-hov/lan( 33-hov/lan( 33-hov/lan( 33-hov/lan( 50-pic/zie(

ρ

ρ

Further references: [36-nor/has, 38-gin/web, 38-whi/joh, 39-owe/qua, 52-lev/tan, 85-ort, 94-tar/jun].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15

Landolt-Börnstein New Series IV/8G

ρ ± σ fit kg ⋅ m−3 831.94 ± 0.85 824.20 ± 0.69 816.18 ± 0.62 813.60 ± 0.61 809.45 ± 0.60

T K

300.00 310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 807.89 ± 0.60 799.32 ± 0.60 790.48 ± 0.59 781.36 ± 0.57 771.97 ± 0.54

T K

350.00 360.00 370.00

ρ ± σ fit kg ⋅ m−3 762.30 ± 0.55 752.36 ± 0.64 742.14 ± 0.84

70

2.1.2 Alkanols, C5 - C6

2-Methyl-3-pentanol

[565-67-3]

C6H14O

MW = 102.18

36

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 6.8420 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.7852 · 10−1 (combined temperature ranges, unweighted). T = 278.15 to 398.15 K ρ = A + BT + CT 2 + DT 3 + … 9.13614 · 102 2.23285 · 10−1 −1.80054 · 10−3

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 293.15 288.95 298.15 298.15 293.15 278.15 288.15 298.15 308.15 318.15 328.15

ρexp ± 2σ est kg ⋅ m−3

824.70 ± 1.00 826.90 ± 1.00 819.30 ± 1.00 818.60 ± 1.00 824.00 ± 1.00 837.11 ± 0.60 829.09 ± 0.60 820.62 ± 0.60 811.80 ± 0.60 802.98 ± 0.60 793.44 ± 0.60

ρexp − ρcalc Ref. (Symbol in Fig. 1) kg ⋅ m−3

0.36 −0.90 −0.83 −1.53 −0.34 0.69 0.64 0.49 0.35 0.58 0.44

12-pic/ken(✕ ) 28-kro/see(✕ ) 36-nor/has(∆) 38-gin/web(✕ ) 38-whi/joh(∇) 40-hov/lan-1( ) 40-hov/lan-1( ) 40-hov/lan-1( ) 40-hov/lan-1( ) 40-hov/lan-1( ) 40-hov/lan-1( )

T K 338.15 348.15 358.15 368.15 378.15 388.15 398.15 293.15 293.15 298.15

ρexp ± 2σ est

ρexp − ρcalc Ref. (Symbol in Fig. 1) kg ⋅ m−3

kg ⋅ m−3

783.78 ± 0.60 773.60 ± 0.60 762.93 ± 0.60 751.71 ± 0.60 739.85 ± 0.60 727.85 ± 0.60 718.58 ± 0.60 823.00 ± 1.00 824.90 ± 1.00 820.08 ± 0.40

0.55 0.49 0.30 −0.07 −0.73 −1.16 1.49 −1.34 0.56 −0.05

40-hov/lan-1( ) 40-hov/lan-1( ) 40-hov/lan-1( ) 40-hov/lan-1( ) 40-hov/lan-1( ) 40-hov/lan-1( ) 40-hov/lan-1( ) 44-hen/mat(✕ ) 50-pic/zie(◆) 85-ort/paz-2( )

Further references: [19-beh].

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15 300.00

ρ ± σ fit kg ⋅ m−3 842.64 ± 0.92 834.97 ± 0.87 826.94 ± 0.83 824.34 ± 0.82 820.13 ± 0.80 818.55 ± 0.80

T K

310.00 320.00 330.00 340.00 350.00 360.00

ρ ± σ fit kg ⋅ m−3 809.80 ± 0.77 800.69 ± 0.73 791.22 ± 0.69 781.39 ± 0.65 771.20 ± 0.62 760.65 ± 0.59

T K

370.00 380.00 390.00 400.00 410.00

ρ ± σ fit kg ⋅ m−3 749.74 ± 0.58 738.46 ± 0.60 726.83 ± 0.68 714.84 ± 0.80 702.49 ± 0.99

cont.

Landolt-Börnstein New Series IV/8G

71

ρ

ρ

2.1.2 Alkanols, C5 - C6

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

3-Methyl-1-pentanol

[589-35-5]

C6H14O

MW = 102.18

37

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 8.2830 · 10−1 (combined temperature ranges, weighted), σc,uw = 2.1862 · 10−1 (combined temperature ranges, unweighted). Coefficient A B C

T = 278.15 to 423.15 K ρ = A + BT + CT 2 + DT 3 + … 9.12528 · 102 7.80681 · 10−2 −1.29987 · 10−3

cont.

Landolt-Börnstein New Series IV/8G

72

2.1.2 Alkanols, C5 - C6

3-Methyl-1-pentanol (cont.) Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

−3

kg ⋅ m

293.65 302.15 313.15 333.15 353.15 298.15 293.15 278.15 288.15 298.15 308.15 318.15 328.15 1)

826.20 ± 2.00 819.30 ± 2.00 810.70 ± 2.00 796.60 ± 2.00 781.20 ± 2.00 820.50 ± 0.50 824.20 ± 0.50 833.26 ± 0.60 826.00 ± 0.60 818.68 ± 0.60 811.58 ± 0.60 804.82 ± 0.60 797.38 ± 0.60

ρexp − ρcalc −3

kg ⋅ m

2.84 1.85 1.19 2.33 3.22 0.25 0.49 −0.42 −1.09 −1.57 −1.57 −0.97 −0.79

Ref. (Symbol in Fig. 1) 1)

08-har 08-har(✕ ) 08-har(✕ ) 08-har(✕ ) 08-har1) 27-nor/cor( ) 36-oli(∆) 40-hov/lan(∇) 40-hov/lan(∇) 40-hov/lan(∇) 40-hov/lan(∇) 40-hov/lan(∇) 40-hov/lan(∇)

T K

338.15 348.15 358.15 368.15 378.15 388.15 398.15 408.15 418.15 423.15 293.15 298.15

ρexp ± 2σ est

ρexp − ρcalc

−3

kg ⋅ m

Ref. (Symbol in Fig. 1)

789.62 ± 0.60 781.71 ± 0.60 773.50 ± 0.60 765.18 ± 0.60 756.64 ± 0.60 747.82 ± 0.60 737.26 ± 0.60 727.23 ± 0.60 717.48 ± 0.60 712.58 ± 0.60 824.10 ± 0.60 821.70 ± 0.50

−0.67 −0.44 −0.25 0.09 0.47 0.83 −0.29 −0.62 −0.41 −0.23 0.39 1.45

40-hov/lan(∇) 40-hov/lan(∇) 40-hov/lan(∇) 40-hov/lan(∇) 40-hov/lan(∇) 40-hov/lan(∇) 40-hov/lan(∇) 40-hov/lan(∇) 40-hov/lan(∇) 40-hov/lan(∇) 52-coo(◆) 59-pin/lar( )

kg ⋅ m

−3

Not included in Fig. 1.

ρ

ρ

Further references: [12-ipa, 41-boh, 41-hus/age, 43-boh, 50-pic/zie].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont. Landolt-Börnstein New Series IV/8G

2.1.2 Alkanols, C5 - C6

73

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15 300.00 310.00

ρ ± σ fit kg ⋅ m−3

ρ ± σ fit kg ⋅ m−3

T K

838.85 ± 1.08 832.48 ± 1.07 825.85 ± 1.05 823.71 ± 1.03 820.25 ± 1.02 818.96 ± 1.02 811.81 ± 0.99

804.40 ± 1.03 796.73 ± 1.01 788.81 ± 0.96 780.62 ± 0.87 772.17 ± 0.78 763.46 ± 0.68 754.49 ± 0.59

320.00 330.00 340.00 350.00 360.00 370.00 380.00

(R)-3-Methyl-1-pentanol

T K

[70224-28-1]

390.00 400.00 410.00 420.00 430.00

ρ ± σ fit kg ⋅ m−3 745.26 ± 0.53 735.78 ± 0.52 726.03 ± 0.58 716.02 ± 0.71 705.75 ± 0.93

C6H14O

MW = 102.18

38

C6H14O

MW = 102.18

39

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.020. Coefficient ρ = A + BT 1060.34 A B −0.800 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est T K kg ⋅ m−3 292.95 826.0 ± 0.5 298.15 821.8 ± 0.5

ρexp − ρcalc

Ref.

kg ⋅ m−3

0.02 −0.02

59-pin/lar 59-pin/lar

Table 3. Recommended values. T K 290.00 293.15 298.15

ρexp ± 2σ est kg ⋅ m−3

828.3 ± 0.5 825.8 ± 0.5 821.8 ± 0.5

3-Methyl-2-pentanol

[565-60-6]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 3.8542 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.6563 · 10−1 (combined temperature ranges, unweighted). Coefficient A B C

T = 278.15 to 398.15 K ρ = A + BT + CT 2 + DT 3 + … 9.72247 · 102 −1.48421 · 10−1 −1.16182 · 10−3 cont.

Landolt-Börnstein New Series IV/8G

74

2.1.2 Alkanols, C5 - C6

3-Methyl-2-pentanol (cont.)

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

−3

kg ⋅ m

830.70 ± 1.00 824.00 ± 1.00 826.40 ± 1.00 823.50 ± 1.00 823.10 ± 1.00 841.51 ± 0.50 833.26 ± 0.50 824.73 ± 0.50 816.31 ± 0.50

0.15 −0.72 1.68 −1.22 −1.62 0.43 0.25 0.01 0.12

kg ⋅ m

291.15 298.15 298.15 298.15 298.15 278.15 288.15 298.15 308.15

ρexp − ρcalc

−3

Ref. (Symbol in Fig. 1) 1883-wis(∇) 36-nor/has(∆) 36-nor/has(∆) 36-nor/has(∆) 38-gin/web( ) 41-hov/lan( ) 41-hov/lan( ) 41-hov/lan( ) 41-hov/lan( )

T K

318.15 328.15 338.15 348.15 358.15 368.15 378.15 388.15 398.15

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

807.50 ± 0.50 798.53 ± 0.50 789.32 ± 0.50 779.86 ± 0.50 770.28 ± 0.50 760.33 ± 0.50 750.17 ± 0.50 739.63 ± 0.50 728.86 ± 0.50

0.07 0.10 0.11 0.11 0.22 0.19 0.19 0.03 −0.12

kg ⋅ m

Ref. (Symbol in Fig. 1)

) ) ) ) ) ) ) ) )

41-hov/lan( 41-hov/lan( 41-hov/lan( 41-hov/lan( 41-hov/lan( 41-hov/lan( 41-hov/lan( 41-hov/lan( 41-hov/lan(

ρ

ρ

Further references: [01-zel/zel, 50-pic/zie, 84-bra/pin, 85-ort, 94-tar/jun].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont.

Landolt-Börnstein New Series IV/8G

2.1.2 Alkanols, C5 - C6

75

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ).

ρ ± σ fit kg ⋅ m−3

T K

T K

847.48 ± 0.90 839.60 ± 0.82 831.50 ± 0.77 828.89 ± 0.75 824.72 ± 0.73 823.16 ± 0.73

270.00 280.00 290.00 293.15 298.15 300.00

310.00 320.00 330.00 340.00 350.00 360.00

3-Methyl-3-pentanol

ρ ± σ fit kg ⋅ m−3 814.59 ± 0.70 805.78 ± 0.67 796.75 ± 0.65 787.48 ± 0.62 777.98 ± 0.59 768.24 ± 0.56

[77-74-7]

ρ ± σ fit kg ⋅ m−3

T K

370.00 380.00 390.00 400.00 410.00

C6H14O

758.28 ± 0.53 748.08 ± 0.51 737.65 ± 0.52 726.99 ± 0.55 716.09 ± 0.64

MW = 102.18

40

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 5.7626 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.1588 · 10−1 (combined temperature ranges, unweighted). T = 273.15 to 338.15 K ρ = A + BT + CT 2 + DT 3 + … 9.06284 · 102 3.36695 · 10−1 −2.05718 · 10−3

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 273.15 298.15 273.15 298.15 308.15 318.15 328.15 338.15 293.15 298.15 273.15 280.15 293.15 1)

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

845.20 ± 0.80 824.20 ± 0.50 844.50 ± 1.00 821.50 ± 1.00 812.20 ± 1.00 803.10 ± 1.00 794.00 ± 1.00 784.80 ± 1.00 828.60 ± 0.40 824.30 ± 0.40 844.00 ± 2.00 837.10 ± 2.00 827.90 ± 2.00

0.44 0.40 −0.26 −2.30 −2.49 −2.08 −1.25 −0.11 0.40 0.50 −0.76 −2.05 −0.30

kg ⋅ m

Ref. (Symbol in Fig. 1) 21-par/sim(✕ ) 38-gin/web(∇) 39-owe/qua(✕ ) 39-owe/qua1) 39-owe/qua1) 39-owe/qua1) 39-owe/qua(✕ ) 39-owe/qua(✕ ) 47-how/mea( ) 47-how/mea( ) 48-zal(✕ ) 48-zal1) 48-zal1)

T K 298.15 293.15 298.15 300.15 302.15 304.15 306.15 308.15 283.15 298.15 313.15 323.15 298.15

ρexp ± 2σ est

ρexp − ρcalc

−3

kg ⋅ m

Ref. (Symbol in Fig. 1)

823.00 ± 0.40 827.96 ± 0.50 823.63 ± 0.50 821.84 ± 0.50 819.99 ± 0.50 818.32 ± 0.50 816.50 ± 0.50 814.77 ± 0.50 837.20 ± 0.50 824.50 ± 0.50 810.54 ± 0.50 800.95 ± 0.50 823.63 ± 0.30

−0.80 −0.24 −0.17 −0.17 −0.22 −0.07 −0.05 0.08 0.51 0.70 0.55 0.69 −0.17

84-bra/pin(∆) 85-ort(✕ ) 85-ort(✕ ) 85-ort(✕ ) 85-ort(✕ ) 85-ort(✕ ) 85-ort(✕ ) 85-ort(✕ ) 88-cac/cos(◆) 88-cac/cos(◆) 88-cac/cos(◆) 88-cac/cos(◆) 94-tar/jun( )

kg ⋅ m

−3

Not included in Fig. 1.

Further references: [1887-ref, 19-eyk, 27-nor/cor, 35-sav, 36-nor/has, 40-hov/lan-1, 50-pic/zie, 52-van, 55-soe/fre, 56-sok/fed]. cont.

Landolt-Börnstein New Series IV/8G

76

2.1.2 Alkanols, C5 - C6

ρ

ρ

3-Methyl-3-pentanol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15

ρ ± σ fit kg ⋅ m−3

T K

847.22 ± 1.55 839.28 ± 0.87 830.92 ± 0.52 828.20 ± 0.47

4-Methyl-1-pentanol

298.15 300.00 310.00 320.00

ρ ± σ fit kg ⋅ m−3

T K

823.80 ± 0.44 822.15 ± 0.44 812.96 ± 0.53 803.37 ± 0.72 [626-89-1]

330.00 340.00 350.00

C6H14O

ρ ± σ fit kg ⋅ m−3 793.37 ± 0.95 782.95 ± 1.17 772.12 ± 1.36

MW = 102.18

41

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 3.9343 · 10−1 (combined temperature ranges, weighted), σc,uw = 8.2317 · 10−2 (combined temperature ranges, unweighted). Coefficient A B C

T = 273.15 to 423.15 K ρ = A + BT + CT 2 + DT 3 + … 9.17775 · 102 −2.40364 · 10−2 −1.13490 · 10−3 cont.

Landolt-Börnstein New Series IV/8G

2.1.2 Alkanols, C5 - C6

77

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

−3

kg ⋅ m

827.00 ± 1.00 814.00 ± 1.00 813.10 ± 0.60 823.74 ± 0.50 816.45 ± 0.50 809.38 ± 0.50 802.44 ± 0.50 794.91 ± 0.50 787.40 ± 0.50 779.66 ± 0.50 771.78 ± 0.50

0.47 −0.23 −0.10 0.45 −0.17 −0.34 −0.16 −0.34 −0.28 −0.22 −0.07

kg ⋅ m

273.15 291.65 293.15 278.15 288.15 298.15 308.15 318.15 328.15 338.15 348.15

ρexp − ρcalc

−3

Ref. (Symbol in Fig. 1) 19-beh(∇) 19-beh(∇) 36-oli(∆) 40-hov/lan( 40-hov/lan( 40-hov/lan( 40-hov/lan( 40-hov/lan( 40-hov/lan( 40-hov/lan( 40-hov/lan(

) ) ) ) ) ) ) )

T K

358.15 368.15 378.15 388.15 398.15 408.15 418.15 423.15 293.15 293.15

ρexp ± 2σ est −3

kg ⋅ m

763.76 ± 0.50 755.24 ± 0.50 746.81 ± 0.60 737.78 ± 0.60 728.48 ± 0.60 718.78 ± 0.60 708.98 ± 0.60 703.90 ± 0.60 812.90 ± 0.50 814.20 ± 1.50

ρexp − ρcalc kg ⋅ m−3

0.17 0.13 0.41 0.32 0.18 −0.13 −0.31 −0.49 −0.30 1.00

Ref. (Symbol in Fig. 1)

) ) ) ) ) ) ) ) )

40-hov/lan( 40-hov/lan( 40-hov/lan( 40-hov/lan( 40-hov/lan( 40-hov/lan( 40-hov/lan( 40-hov/lan( 50-pic/zie( 52-coo(◆)

ρ

ρ

Further references: [02-gri/tis, 27-nor/cor, 41-hus/age].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont. Landolt-Börnstein New Series IV/8G

78

2.1.2 Alkanols, C5 - C6

4-Methyl-1-pentanol (cont.) Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ).

ρ ± σ fit kg ⋅ m−3

T K

T K

828.55 ± 0.92 822.07 ± 0.82 815.36 ± 0.74 813.20 ± 0.72 809.72 ± 0.69 808.42 ± 0.68 801.26 ± 0.63

270.00 280.00 290.00 293.15 298.15 300.00 310.00

320.00 330.00 340.00 350.00 360.00 370.00 380.00

4-Methyl-2-pentanol

ρ ± σ fit kg ⋅ m−3 793.87 ± 0.59 786.25 ± 0.57 778.41 ± 0.55 770.34 ± 0.54 762.04 ± 0.53 753.51 ± 0.53 744.76 ± 0.54

[108-11-2]

ρ ± σ fit kg ⋅ m−3

T K

390.00 400.00 410.00 420.00 430.00

C6H14O

735.78 ± 0.56 726.58 ± 0.59 717.14 ± 0.64 707.48 ± 0.71 697.60 ± 0.80

MW = 102.18

42

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 3.2132 · 10−1 (combined temperature ranges, weighted), σc,uw = 4.5436 · 10−2 (combined temperature ranges, unweighted). T = 273.15 to 405.15 K ρ = A + BT + CT 2 + DT 3 + … 9.40784 · 102 −1.09111 · 10−1 −1.18327 · 10−3

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 273.15 298.15 278.15 288.15 298.15 308.15 318.15 328.15 338.15 348.15 358.15 368.15 378.15 388.15

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

823.00 ± 1.00 803.40 ± 0.60 819.07 ± 0.50 811.18 ± 0.50 803.04 ± 0.50 794.82 ± 0.50 786.37 ± 0.50 777.69 ± 0.50 768.95 ± 0.50 759.87 ± 0.50 749.60 ± 0.50 739.95 ± 0.50 730.12 ± 0.50 720.04 ± 0.50

0.30 0.33 0.18 0.08 −0.03 0.02 0.07 0.13 0.36 0.49 −0.33 −0.29 −0.20 −0.12

kg ⋅ m

Ref. (Symbol in Fig. 1) 09-gue(✕ ) 38-gin/web(✕ ) 38-hov/lan(∇) 38-hov/lan(∇) 38-hov/lan(∇) 38-hov/lan(∇) 38-hov/lan(∇) 38-hov/lan(∇) 38-hov/lan(∇) 38-hov/lan(∇) 38-hov/lan(∇) 38-hov/lan(∇) 38-hov/lan(∇) 38-hov/lan(∇)

T K 398.15 405.15 293.15 292.65 293.15 298.15 293.15 298.15 300.15 302.15 304.15 306.15 308.15 298.15

ρexp ± 2σ est −3

kg ⋅ m

710.12 ± 0.50 702.10 ± 0.50 807.50 ± 0.50 807.50 ± 0.60 806.90 ± 0.50 802.72 ± 0.40 806.99 ± 0.40 802.98 ± 0.40 801.29 ± 0.40 799.64 ± 0.40 798.01 ± 0.40 796.38 ± 0.40 794.69 ± 0.40 802.98 ± 0.30

ρexp − ρcalc kg ⋅ m−3

0.35 −0.25 0.39 −0.01 −0.21 −0.35 −0.12 −0.09 −0.14 −0.15 −0.13 −0.09 −0.11 −0.09

Ref. (Symbol in Fig. 1) 38-hov/lan(∇) 38-hov/lan(∇) 44-hen/mat(✕ ) 49-ken/str(✕ ) 68-ano(◆) 84-bra/pin(∆) 85-ort( ) 85-ort( ) 85-ort( ) 85-ort( ) 85-ort( ) 85-ort( ) 85-ort( ) 94-tar/jun( )

cont.

Landolt-Börnstein New Series IV/8G

2.1.2 Alkanols, C5 - C6

79

ρ

ρ

Further references: [11-pic/ken, 12-gue, 14-vav, 19-beh, 21-bru/cre, 23-bru, 33-van, 38-whi/joh, 39-dup/dar, 47-tuo/guy, 48-wei, 50-pic/zie, 53-ano-1, 58-ano-5, 58-rao/ram].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15 300.00

Landolt-Börnstein New Series IV/8G

ρ ± σ fit kg ⋅ m−3 825.06 ± 0.89 817.46 ± 0.68 809.63 ± 0.54 807.11 ± 0.50 803.07 ± 0.46 801.56 ± 0.45

T K

310.00 320.00 330.00 340.00 350.00 360.00

ρ ± σ fit kg ⋅ m−3 793.25 ± 0.42 784.70 ± 0.42 775.92 ± 0.44 766.90 ± 0.48 757.64 ± 0.51 748.15 ± 0.55

T K

370.00 380.00 390.00 400.00 410.00 420.00

ρ ± σ fit kg ⋅ m−3 738.42 ± 0.57 728.46 ± 0.58 718.26 ± 0.57 707.82 ± 0.55 697.14 ± 0.52 686.23 ± 0.53

2.1.3 Alkanols, C7

81

2.1.3 Alkanols, C7 2,2-Dimethyl-1-pentanol

[2370-12-9]

C7H16O

MW = 116.2

43

C7H16O

MW = 116.2

44

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 65-shu/puz 837.9 ± 1.0 2,2-Dimethyl-3-pentanol

[3970-62-5]

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 0.493. ρ = A + BT Coefficient 1060.34 A B −0.800 Table 2. Experimental values with uncertainties and deviation from calculated values. T K

ρexp ± 2σ est −3

kg ⋅ m

293.15 824.6 ± 2.0 293.15 824.0 ± 2.0 298.15 822.4 ± 1.0 1)

ρexp − ρcalc

T K

Ref.

−3

kg ⋅ m

−1.22 −1.82 0.58

1)

13-fav 29-edg/cal1) 38-gin/hau

ρexp ± 2σ est −3

kg ⋅ m

293.15 825.4 ± 0.6 293.15 826.4 ± 1.0 293.15 828.1 ± 2.0

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−0.42 0.58 2.28

49-boo/gre 50-pic/zie 55-gay/cau1)

Not included in calculation of linear coefficients.

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 290.00 828.3 ± 0.8 293.15 825.8 ± 0.6 298.15 821.8 ± 0.7 2,3-Dimethyl-1-pentanol

[10143-23-4]

C7H16O

MW = 116.2

45

C7H16O

MW = 116.2

46

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 296.15 31-lev/mar-2 836.0 ± 2.0 2,3-Dimethyl-2-pentanol

[4911-70-0]

Table 1. Fit with estimated B coefficient for 5 accepted points. Deviation σw = 0.857. ρ = A + BT Coefficient 1060.84 A B −0.780 cont. Landolt-Börnstein New Series IV/8G

82

2.1.3 Alkanols, C7

2,3-Dimethyl-2-pentanol (cont.) Table 2. Experimental values with uncertainties and deviation from calculated values. T K 293.15 298.15 298.15 1)

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

803.0 ± 5.0 828.5 ± 1.0 827.6 ± 1.0

−29.18 0.22 −0.68

Ref. 29-edg/cal1) 36-nor/has 36-nor/has

T K 298.15 293.15 293.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

830.7 ± 2.0 832.4 ± 1.0 830.7 ± 2.0

2.42 0.22 −1.48

Ref. 38-gin/hau 43-jam 50-pic/zie

Not included in calculation of linear coefficients.

Table 3. Recommended values. T K 290.00 293.15 298.15

ρexp ± 2σ est kg ⋅ m−3

834.6 ± 1.5 832.2 ± 1.4 828.3 ± 1.4

l-2,3-Dimethyl-2-pentanol

[28357-68-8]

C7H16O

MW = 116.2

47

C7H16O

MW = 116.2

48

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

836.0 ± 1.0

57-luk/lan

2,3-Dimethyl-3-pentanol

[595-41-5]

Table 1. Fit with estimated B coefficient for 6 accepted points. Deviation σw = 0.901. ρ = A + BT Coefficient 1075.79 A B −0.800 Table 2. Experimental values with uncertainties and deviation from calculated values. T K 273.15 293.15 293.15 298.15 1)

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

858.6 ± 1.0 841.5 ± 1.0 833.0 ± 4.0 836.6 ± 1.0

1.33 0.23 −8.27 −0.67

Ref. 21-par/sim 21-par/sim 33-whi/eve1) 36-nor/has

T K 298.15 298.15 293.15 293.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

838.2 ± 1.0 836.5 ± 1.0 840.2 ± 1.0 832.0 ± 4.0

0.93 −0.77 −1.07 −9.27

Ref. 36-nor/has 38-gin/hau 50-pic/zie 56-sok/fed1)

Not included in calculation of linear coefficients.

Table 3. Recommended values. T K 270.00 280.00 290.00

ρexp ± 2σ est −3

kg ⋅ m

859.8 ± 1.6 851.8 ± 1.3 843.8 ± 1.1

T K 293.15 298.15

ρexp ± 2σ est kg ⋅ m−3

841.3 ± 1.1 837.3 ± 1.2

Landolt-Börnstein New Series IV/8G

2.1.3 Alkanols, C7 2,4-Dimethyl-1-pentanol

[6305-71-1]

83 C7H16O

MW = 116.2

49

C7H16O

MW = 116.2

50

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.500. Coefficient ρ = A + BT 1054.02 A B −0.800 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

293.15 298.15 298.15 293.15 1)

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−3

kg ⋅ m

793.0 ± 15.0 821.0 ± 5.0 816.0 ± 2.0 819.0 ± 2.0

−26.50 5.50 0.50 −0.50

31-chu/mar1) 32-mor/har1) 35-lev/mar 39-gol/tay

Not included in calculation of linear coefficients.

Table 3. Recommended values. ρexp ± 2σ est

T K

kg ⋅ m−3

822.0 ± 1.2 819.5 ± 1.1 815.5 ± 1.1

290.00 293.15 298.15

2,4-Dimethyl-2-pentanol

[625-06-9]

Table 1. Fit with estimated B coefficient for 7 accepted points. Deviation σw = 0.680. Coefficient ρ = A + BT 1034.29 A B −0.760 Table 2. Experimental values with uncertainties and deviation from calculated values. T K

293.15 273.15 293.15 293.15 288.15 298.15 1)

ρexp ± 2σ est −3

kg ⋅ m

815.7 ± 3.0 832.5 ± 3.0 812.2 ± 1.0 810.3 ± 1.0 814.8 ± 1.0 810.0 ± 2.0

ρexp − ρcalc

Ref.

−3

kg ⋅ m

4.20 5.80 0.70 −1.20 −0.50 2.30

09-kho1) 09-kho1) 24-cha/deg 31-deg 31-deg 38-gin/hau1)

T K

293.15 293.15 293.15 293.15 293.15

ρexp ± 2σ est −3

kg ⋅ m

811.0 ± 1.0 812.2 ± 1.0 811.9 ± 1.0 811.9 ± 1.0 814.6 ± 2.0

ρexp − ρcalc

Ref.

kg ⋅ m−3

−0.50 0.70 0.40 0.40 3.10

38-whi/joh 50-pic/zie 57-pet/sus 59-pet/zak-1 66-are/tav1)

Not included in calculation of linear coefficients.

cont.

Landolt-Börnstein New Series IV/8G

84

2.1.3 Alkanols, C7

2,4-Dimethyl-2-pentanol (cont.) Table 3. Recommended values. ρexp ± 2σ est

T K

kg ⋅ m−3

821.5 ± 1.5 813.9 ± 0.9 811.5 ± 0.9 807.7 ± 1.1

280.00 290.00 293.15 298.15

2,4-Dimethyl-3-pentanol

[600-36-2]

C7H16O

MW = 116.2

51

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 1.0054 (combined temperature ranges, weighted), σc,uw = 2.2149 · 10−1 (combined temperature ranges, unweighted). T = 290.15 to 394.75 K ρ = A + BT + CT 2 + DT 3 + … 1.11751 · 103 −9.81289 · 10−1

Coefficient A B

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

290.15 293.15 298.15 293.15 293.15 303.15 293.15 293.15

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

832.30 ± 1.00 828.80 ± 1.00 825.40 ± 1.00 831.00 ± 1.00 828.80 ± 0.60 819.20 ± 2.00 829.40 ± 1.00 830.40 ± 0.50

−0.49 −1.04 0.46 1.16 −1.04 −0.83 −0.44 0.56

kg ⋅ m

Ref. (Symbol in Fig. 1) 1876-mun(✕ ) 1891-pol(✕ ) 38-gin/hau(◆) 38-whi/joh(✕ ) 39-gol/tay(∆) 48-wei(✕ ) 50-pic/zie(✕ ) 52-coo( )

T K

293.15 306.95 316.55 335.85 353.55 365.75 378.65 394.75

ρexp ± 2σ est

ρexp − ρcalc

−3

kg ⋅ m

Ref. (Symbol in Fig. 1)

830.20 ± 0.50 815.30 ± 1.00 808.10 ± 1.00 789.30 ± 1.00 771.60 ± 1.00 758.70 ± 1.00 745.50 ± 1.00 729.20 ± 1.00

0.36 −1.00 1.22 1.36 1.03 0.10 −0.44 −0.94

53-raz/old( ) 63-tho/mea(∇) 63-tho/mea(∇) 63-tho/mea(∇) 63-tho/mea(∇) 63-tho/mea(∇) 63-tho/mea(∇) 63-tho/mea(∇)

−3

kg ⋅ m

Further references: [44-hus/awu, 49-naz/pin]. Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

290.00 293.15 298.15 300.00 310.00

ρ ± σ fit kg ⋅ m−3 832.93 ± 0.90 829.84 ± 0.90 824.94 ± 0.90 823.12 ± 0.90 813.31 ± 0.90

T K

320.00 330.00 340.00 350.00 360.00

ρ ± σ fit kg ⋅ m−3 803.50 ± 0.91 793.68 ± 0.93 783.87 ± 0.95 774.06 ± 0.97 764.24 ± 1.00

T K

370.00 380.00 390.00 400.00

ρ ± σ fit kg ⋅ m−3 754.43 ± 1.03 744.62 ± 1.06 734.81 ± 1.10 724.99 ± 1.14

cont. Landolt-Börnstein New Series IV/8G

85

ρ

ρ

2.1.3 Alkanols, C7

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

3,3-Dimethyl-1-pentanol

[19264-94-9]

C7H16O

MW = 116.2

52

C7H16O

MW = 116.2

53

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

832.0 ± 1.0

45-sch

3,3-Dimethyl-2-pentanol

[19781-24-9]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

827.0 ± 1.5

Landolt-Börnstein New Series IV/8G

29-edg/cal

86

2.1.3 Alkanols, C7

3,4-Dimethyl-1-pentanol

[6570-87-2]

C7H16O

MW = 116.2

54

C7H16O

MW = 116.2

55

C7H16O

MW = 116.2

56

C7H16O

MW = 116.2

57

Table 1. Experimental values with uncertainties. T K 297.15 293.15 325.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

819.0 ± 2.0 834.5 ± 2.0 803.5 ± 2.0

41-hus/age 47-det/cra 60-tsu/kis

3,4-Dimethyl-2-pentanol

[64502-86-9]

Table 1. Experimental value with uncertainty. T K 294.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

836.0 ± 2.0

19-wil/hat

4,4-Dimethyl-1-pentanol

[3121-79-7]

Table 1. Experimental and recommended values with uncertainties. T K 290.15 293.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

kg ⋅ m−3

820.0 ± 2.0 815.2 ± 1.0 815.0 ± 1.0 815.1 ± 1.0

49-mal/vol1) 31-hom 33-whi/hom-1 Recommended

Not included in calculation of recommended value.

4,4-Dimethyl-2-pentanol

[6144-93-0]

Table 1. Experimental and recommended values with uncertainties. T K 293.15 293.15 293.15

ρexp ± 2σ est

T K 293.15 293.15 293.15

Ref.

kg ⋅ m−3

811.5 ± 1.0 812.0 ± 1.0 811.5 ± 1.0

33-whi/hom 33-whi/hom-1 33-whi/kru

2-Ethyl-2-methyl-1-butanol

ρexp ± 2σ est

Ref.

kg ⋅ m−3

811.3 ± 1.0 813.3 ± 1.0 811.9 ± 1.2

[18371-13-6]

C7H16O

52-coo 55-gay/cau Recommended

MW = 116.2

58

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 1.550. Coefficient ρ = A + BT 1055.31 A B −0.780 cont.

Landolt-Börnstein New Series IV/8G

2.1.3 Alkanols, C7

87

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 293.15 273.15

ρexp ± 2σ est

ρexp − ρcalc kg ⋅ m

kg ⋅ m

828.2 ± 1.0 840.7 ± 1.0

Ref.

−3

−3

1.55 −1.55

25-fav/zal 25-fav/zal

Table 3. Recommended values. ρexp ± 2σ est

T K 270.00 280.00 290.00 293.15 298.15

kg ⋅ m−3

844.7 ± 1.9 836.9 ± 1.8 829.1 ± 1.8 826.7 ± 1.9 822.7 ± 1.9

2-Ethyl-3-methyl-1-butanol

[32444-34-1]

C7H16O

MW = 116.2

59

C7H16O

MW = 116.2

60

C7H16O

MW = 116.2

61

Table 1. Experimental and recommended values with uncertainties. T K 298.15 298.15 298.15 298.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

832.7 ± 1.0 832.6 ± 0.8 832.6 ± 1.0 832.6 ± 0.8

56-sar/new 59-tsu/hay 60-tsu/kis Recommended

2-Ethyl-1-pentanol

[27522-11-8]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est

T K

298.15 298.15 298.15 298.15 1)

Ref.

kg ⋅ m−3

832.0 ± 3.0 828.0 ± 2.0 829.6 ± 2.0 828.8 ± 2.1

32-mor/har1) 36-lev/rot-1 50-ada/van Recommended

Not included in calculation of recommended value.

3-Ethyl-2-pentanol

[609-27-8]

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.200. Coefficient ρ = A + BT 1071.82 A B −0.800 cont.

Landolt-Börnstein New Series IV/8G

88

2.1.3 Alkanols, C7

3-Ethyl-2-pentanol (cont.) Table 2. Experimental values with uncertainties and deviation from calculated values. T K

273.15 298.15

ρexp ± 2σ est

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−3

kg ⋅ m

853.1 ± 2.0 833.5 ± 2.0

−0.20 0.20

07-fou/tif 29-luc

Table 3. Recommended values. ρexp ± 2σ est

T K 270.00 280.00 290.00 293.15 298.15

kg ⋅ m−3

855.8 ± 2.4 847.8 ± 1.9 839.8 ± 1.9 837.3 ± 2.0 833.3 ± 2.2

3-Ethyl-3-pentanol

[597-49-9]

C7H16O

MW = 116.2

62

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 5.5395 · 10−1 (combined temperature ranges, weighted), σc,uw = 3.5871 · 10−1 (combined temperature ranges, unweighted). T = 273.15 to 338.15 K ρ = A + BT + CT 2 + DT 3 + … 8.65425 · 102 7.69225 · 10−1 −2.87450 · 10−3

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 287.05 298.15 295.54 273.15 298.15 308.15 318.15 328.15 1)

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

849.00 ± 2.00 841.30 ± 1.00 840.70 ± 2.00 860.30 ± 1.00 836.70 ± 1.00 827.30 ± 1.00 817.50 ± 1.00 808.00 ± 1.00

−0.38 2.05 −0.99 −0.77 −2.55 −2.21 −1.70 −0.31

kg ⋅ m

Ref. (Symbol in Fig. 1) 19-eyk(✕ ) 29-luc(∇) 32-boe/wil(◆) 39-owe/qua1) 39-owe/qua1) 39-owe/qua1) 39-owe/qua(∆) 39-owe/qua(∆)

T K 338.15 293.15 273.15 288.15 303.15 293.15 298.15

ρexp ± 2σ est −3

kg ⋅ m

798.20 ± 1.00 842.00 ± 2.00 861.18 ± 0.40 848.29 ± 0.40 834.83 ± 0.40 845.09 ± 2.00 839.56 ± 0.40

ρexp − ρcalc kg ⋅ m−3

1.35 −1.90 0.11 −0.12 0.38 1.19 0.31

Ref. (Symbol in Fig. 1) 39-owe/qua(∆) 53-gru/ost(✕ ) 55-tim/hen( ) 55-tim/hen( ) 55-tim/hen( ) 56-lib/lap-1(✕ ) 88-cac/cos( )

Not included in Fig. 1.

Further references: [29-edg/cal, 50-pic/zie, 55-soe/fre, 62-and/kuk-1]. cont.

Landolt-Börnstein New Series IV/8G

89

ρ

ρ

2.1.3 Alkanols, C7

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15

Landolt-Börnstein New Series IV/8G

ρ ± σ fit kg ⋅ m−3 863.57 ± 1.50 855.45 ± 1.47 846.76 ± 1.38 843.90 ± 1.37

T K

298.15 300.00 310.00 320.00

ρ ± σ fit kg ⋅ m−3 839.25 ± 1.29 837.49 ± 1.25 827.65 ± 0.95 817.23 ± 0.73

T K

330.00 340.00 350.00

ρ ± σ fit kg ⋅ m−3 806.24 ± 0.87 794.67 ± 1.54 782.53 ± 2.94

90

2.1.3 Alkanols, C7

1-Heptanol

[111-70-6]

C7H16O

MW = 116.2

63

Tc = 632.50 K [89-tej/lee] ρc = 267.00 kg·m−3 [89-tej/lee] Table 1. Coefficients for the polynomial expansion equations. Standard deviations (see introduction): σ = 7.2440 · 10−1 (low temperature range), σc,w = (2.0233 · 10−1 combined temperature ranges, weighted), σc,uw = 3.3667 · 10−1 (combined temperature ranges, unweighted).

T = 273.15 to 510.00 K ρ = A + BT + CT 2 + DT 3 + …

Coefficient

9.98526 · 102 −6.23212 · 10−1 4.74025 · 10−4 −1.34624 · 10−6

A B C D

T = 510.00 to 632.50 K ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)] [ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] 9.10034 · 10−1 −1.32340 · 10−2 8.23480 · 10−5 −1.83963 · 10−7

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 273.15 273.15 288.15 288.15 303.15 303.15 273.15 298.15 273.15 288.15 303.15 273.15 273.15 293.15 313.15 333.15 353.15 373.15 393.15 413.15 433.15 453.15 473.15 493.15 513.15 1)

ρexp ± 2σ est

ρexp − ρcalc

−3

kg ⋅ m

Ref. (Symbol in Fig. 1)

836.20 ± 0.50 836.20 ± 1.00 825.99 ± 0.50 825.99 ± 1.00 815.81 ± 0.50 818.81 ± 1.00 836.32 ± 0.20 819.13 ± 0.20 836.04 ± 0.30 825.80 ± 0.30 815.57 ± 0.30 836.50 ± 0.10 839.00 ± 1.50 824.00 ± 1.50 809.00 ± 1.50 794.00 ± 1.50 778.00 ± 1.50 762.00 ± 1.50 745.00 ± 1.50 726.00 ± 1.50 707.00 ± 1.50 688.00 ± 1.50 669.00 ± 1.50 648.00 ± 1.50 626.00 ± 1.50

−0.03 −0.03 −0.11 −0.11 0.15 3.15 0.09 −0.04 −0.19 −0.30 −0.09 0.27 2.77 1.35 0.49 0.26 −0.26 −0.03 0.03 −1.02 −1.11 −0.19 1.83 2.99 4.36

31-def(✕ ) 31-def1) 31-def1) 31-def1) 31-def1) 31-def1) 32-ell/rei(◆) 32-ell/rei1) 35-bil/gis(✕ ) 35-bil/gis(✕ ) 35-bil/gis1) 59-mck/ski(∆) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr1) 66-efr(✕ )

kg ⋅ m

−3

T K 533.15 553.15 573.15 593.15 603.15 613.15 618.15 623.15 628.15 298.15 298.15 313.15 298.15 308.15 318.15 333.15 293.15 298.15 303.15 308.15 313.15 318.15 298.15 303.15 323.15

ρexp ± 2σ est −3

kg ⋅ m

600.00 ± 1.50 574.00 ± 1.50 540.00 ± 1.50 496.00 ± 1.50 470.00 ± 1.50 440.00 ± 2.00 420.00 ± 2.00 400.00 ± 5.00 370.00 ± 5.00 819.30 ± 0.25 819.29 ± 0.25 810.47 ± 0.25 819.42 ± 0.20 812.28 ± 0.20 805.10 ± 0.20 794.05 ± 0.20 822.10 ± 0.30 819.50 ± 0.30 815.70 ± 0.30 812.10 ± 0.30 811.20 ± 0.30 804.80 ± 0.30 818.24 ± 0.10 815.72 ± 0.20 801.09 ± 0.10

ρexp − ρcalc kg ⋅ m−3

2.80 3.18 0.23 −3.22 −2.90 −0.03 0.20 4.68 7.80 0.13 0.12 1.96 0.25 0.18 0.22 0.31 −0.55 0.33 0.04 −0.00 2.69 −0.08 −0.93 0.06 −0.12

Ref. (Symbol in Fig. 1) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 76-kow/kas1) 76-kow/kas1) 76-kow/kas(✕ ) 79-dia/tar1) 79-dia/tar(✕ ) 79-dia/tar(✕ ) 79-dia/tar(✕ ) 82-ort1) 82-ort1) 82-ort1) 82-ort1) 82-ort1) 82-ort(✕ ) 84-sak/nak( ) 89-vij/nai(∇) 93-gar/ban-1( )

Not included in Fig. 1.

cont.

Landolt-Börnstein New Series IV/8G

2.1.3 Alkanols, C7

91

Table 2. (cont.) ρexp ± 2σ est

T K

1)

kg ⋅ m

Ref. (Symbol in Fig. 1)

797.68 ± 0.10 793.62 ± 0.10 790.17 ± 0.10 786.06 ± 0.10 781.91 ± 0.10 778.40 ± 0.10 774.25 ± 0.10

0.19 −0.12 0.23 −0.03 −0.29 0.14 −0.03

93-gar/ban-1( 93-gar/ban-1( 93-gar/ban-1( 93-gar/ban-1( 93-gar/ban-1( 93-gar/ban-1( 93-gar/ban-1(

kg ⋅ m

328.15 333.15 338.15 343.15 348.15 353.15 358.15

ρexp − ρcalc

−3

−3

) ) ) ) ) ) )

T K

363.15 373.15 278.15 288.15 298.15 308.15

ρexp ± 2σ est −3

kg ⋅ m

770.31 ± 0.10 762.00 ± 0.10 832.91 ± 0.40 825.96 ± 0.40 819.06 ± 0.40 811.99 ± 0.40

ρexp − ρcalc kg ⋅ m−3

0.06 −0.03 0.03 −0.14 −0.11 −0.11

Ref. (Symbol in Fig. 1)

93-gar/ban-1( ) 93-gar/ban-1( ) 94-rom/pel(✕ ) 94-rom/pel1) 94-rom/pel1) 94-rom/pel1)

Not included in Fig. 1.

ρ

ρ

Further references: [1877-cro, 1877-cro-1, 1880-bru-1, 1884-per, 1884-zan, 1886-gar, 1890-gar, 1893-eyk, 06-car/fer, 09-fal-1, 14-low, 18-lev/tay, 19-beh, 19-eyk, 25-fai-1, 27-nor/cor, 27-ver/coo, 28-har-2, 30-bin/for, 30-err/she, 30-she, 33-ano, 33-but/tho, 34-bur/adk, 34-car/jon, 35-but/ram, 35-mah-1, 37-oli, 41-hus/age, 42-mul, 44-app/dob, 45-add, 48-jon/bow, 48-vog-2, 49-pra/dra, 50-mum/phi, 50-pic/zie, 50-sac/sau, 52-coo, 52-eri-1, 66-rob/edm, 67-gol/per, 70-puz/bul, 73-min/rue, 74-moo/wel, 75-mat/fer, 81-sjo/dyh, 82-ven/dha, 83-fuk/ogi, 83-rau/ste, 85-fer/pin, 85-ogi/ara, 85-ort-1, 85-ort/paz-1, 85-sar/paz, 85-zhu, 86-ash/sri, 86-dew/meh, 87-dew/meh, 88-ort/gar, 89-ala/sal, 89-dew/gup, 90-vij/nai, 91-ram/muk, 93-ami/ara, 93-yan/mae, 94-kum/nai, 94-kum/nai-1, 94-yu /tsa-1, 95-cas/cal, 96-elb].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont. Landolt-Börnstein New Series IV/8G

92

2.1.3 Alkanols, C7

1-Heptanol (cont.) Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ).

ρ ± σ fit kg ⋅ m−3

T K

838.32 ± 0.44 831.64 ± 0.29 824.83 ± 0.18 822.65 ± 0.15 819.17 ± 0.11 817.88 ± 0.11 810.78 ± 0.12 803.52 ± 0.12 796.11 ± 0.12 788.52 ± 0.13 780.75 ± 0.15 772.79 ± 0.23 764.64 ± 0.33

270.00 280.00 290.00 293.15 298.15 300.00 310.00 320.00 330.00 340.00 350.00 360.00 370.00

ρ ± σ fit kg ⋅ m−3

T K

2-Heptanol

756.28 ± 0.44 747.72 ± 0.56 738.93 ± 0.69 729.91 ± 0.83 720.65 ± 0.98 711.16 ± 1.12 701.41 ± 1.27 691.39 ± 1.41 681.11 ± 1.55 670.56 ± 1.69 659.72 ± 1.82 648.58 ± 1.94 637.15 ± 2.05

380.00 390.00 400.00 410.00 420.00 430.00 440.00 450.00 460.00 470.00 480.00 490.00 500.00

[543-49-7]

ρ ± σ fit kg ⋅ m−3

T K

510.00 520.00 530.00 540.00 550.00 560.00 570.00 580.00 590.00 600.00 610.00 620.00 630.00 C7H16O

625.40 ± 2.14 613.39 ± 2.64 601.13 ± 2.72 588.48 ± 2.73 575.19 ± 2.68 560.90 ± 2.62 545.14 ± 2.56 527.28 ± 2.52 506.52 ± 2.51 481.77 ± 2.52 451.29 ± 2.59 411.37 ± 3.78 344.48 ± 5.46 MW = 116.2

64

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 8.0415 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.7660 · 10−1 (combined temperature ranges, unweighted). Coefficient A B C

T = 273.15 to 421.45 K ρ = A + BT + CT 2 + DT 3 + … 9.15825 · 102 4.92881 · 10−2 −1.31078 · 10−3

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

293.15 383.15 295.15 273.15 288.15 293.15 273.15 298.15 303.15 293.15 293.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

818.50 ± 1.00 741.70 ± 1.00 815.30 ± 0.60 831.50 ± 1.00 820.30 ± 1.00 816.70 ± 1.00 832.01 ± 0.50 813.38 ± 0.50 809.80 ± 0.50 819.00 ± 1.50 817.90 ± 0.50

0.87 −0.58 −0.89 0.01 −0.89 −0.93 0.52 −0.62 −0.51 1.37 0.27

Ref. (Symbol in Fig. 1) 11-pic/ken(✕ ) 12-pic/ken(◆) 30-err/she(∇) 30-she(✕ ) 30-she(✕ ) 30-she(✕ ) 32-ell/rei( ) 32-ell/rei( ) 48-wei(∆) 50-pic/zie(✕ ) 52-coo( )

T K

293.15 298.15 303.25 321.15 332.35 348.05 362.45 376.75 393.15 408.45 421.45

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

816.70 ± 1.00 812.90 ± 1.00 811.80 ± 1.00 797.80 ± 1.00 788.00 ± 1.00 774.80 ± 1.00 761.50 ± 1.00 748.50 ± 1.00 732.20 ± 1.00 717.10 ± 1.00 703.50 ± 1.00

−0.93 −1.10 1.57 1.34 0.58 0.61 0.01 0.16 −0.40 −0.18 −0.28

Ref. (Symbol in Fig. 1) 52-pom(✕ ) 52-pom(✕ ) 63-tho/mea(✕ ) 63-tho/mea(✕ ) 63-tho/mea(✕ ) 63-tho/mea(✕ ) 63-tho/mea(✕ ) 63-tho/mea(✕ ) 63-tho/mea(✕ ) 63-tho/mea(✕ ) 63-tho/mea(✕ ) cont.

Landolt-Börnstein New Series IV/8G

2.1.3 Alkanols, C7

93

ρ

ρ

Further references: [09-hen, 09-mas, 13-tho, 49-mal/vol, 62-cuv/nor].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15 300.00 310.00

Landolt-Börnstein New Series IV/8G

ρ ± σ fit kg ⋅ m−3 833.58 ± 0.92 826.86 ± 0.89 819.88 ± 0.88 817.63 ± 0.88 814.00 ± 0.88 812.64 ± 0.89 805.14 ± 0.91

T K

320.00 330.00 340.00 350.00 360.00 370.00 380.00

ρ ± σ fit kg ⋅ m−3 797.37 ± 0.93 789.35 ± 0.95 781.06 ± 0.97 772.51 ± 0.99 763.69 ± 1.00 754.62 ± 1.01 745.28 ± 1.02

T K

390.00 400.00 410.00 420.00 430.00

ρ ± σ fit kg ⋅ m−3 735.68 ± 1.04 725.82 ± 1.08 715.69 ± 1.13 705.30 ± 1.21 694.66 ± 1.33

94

2.1.3 Alkanols, C7

3-Heptanol

[589-82-2]

C7H16O

MW = 116.2

65

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 5.5943 · 10−1 (combined temperature ranges, weighted), σc,uw = 2.3013 · 10−1 (combined temperature ranges, unweighted). T = 273.15 to 416.55 K ρ = A + BT + CT 2 + DT 3 + … 9.65814 · 102 −1.88467 · 10−1 −1.04313 · 10−3

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 298.15 295.15 273.15 288.15 293.15 298.15 293.15 293.15 293.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

815.90 ± 2.00 819.40 ± 0.50 837.00 ± 0.50 825.10 ± 0.50 821.00 ± 0.50 816.50 ± 1.00 820.40 ± 1.00 821.10 ± 0.50 820.90 ± 1.00

−1.00 0.08 0.49 0.20 0.08 −0.40 −0.52 0.18 −0.02

Ref. (Symbol in Fig. 1) 28-dil/luc(✕ ) 30-err/she( ) 30-she( ) 30-she( ) 30-she( ) 50-ada/van(✕ ) 50-pic/zie(◆) 52-coo(∆) 53-ano-1(✕ )

T K 306.95 316.55 335.95 353.55 365.75 378.65 405.55 416.55 298.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

810.00 ± 1.00 802.10 ± 1.00 785.80 ± 1.00 767.40 ± 1.00 758.30 ± 1.00 745.90 ± 1.00 716.60 ± 1.00 708.00 ± 1.00 814.92 ± 2.00

0.32 0.47 1.03 −1.39 0.96 1.01 −1.22 1.69 −1.98

Ref. (Symbol in Fig. 1) 63-tho/mea(∇) 63-tho/mea(∇) 63-tho/mea(∇) 63-tho/mea(∇) 63-tho/mea(∇) 63-tho/mea(∇) 63-tho/mea(∇) 63-tho/mea(∇) 88-tan/luo(✕ )

Further references: [13-pic/ken, 61-tis/sta].

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15 300.00 310.00

ρ ± σ fit kg ⋅ m−3 838.88 ± 0.91 831.26 ± 0.88 823.43 ± 0.87 820.92 ± 0.87 816.90 ± 0.87 815.39 ± 0.87 807.14 ± 0.89

T K

320.00 330.00 340.00 350.00 360.00 370.00 380.00

ρ ± σ fit kg ⋅ m−3 798.69 ± 0.91 790.02 ± 0.93 781.15 ± 0.95 772.07 ± 0.96 762.78 ± 0.97 753.28 ± 0.99 743.57 ± 1.00

T K

390.00 400.00 410.00 420.00 430.00

ρ ± σ fit kg ⋅ m−3 733.65 ± 1.03 723.53 ± 1.07 713.19 ± 1.14 702.65 ± 1.23 691.90 ± 1.36

cont.

Landolt-Börnstein New Series IV/8G

95

ρ

ρ

2.1.3 Alkanols, C7

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

4-Heptanol

[589-55-9]

C7H16O

MW = 116.2

66

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 1.1547 (combined temperature ranges, weighted), σc,uw = 2.3522 · 10−1 (combined temperature ranges, unweighted). Coefficient A B C

T = 273.15 to 416.05 K ρ = A + BT + CT 2 + DT 3 + … 9.10927 · 102 9.60428 · 10−2 −1.40301 · 10−3

cont.

Landolt-Börnstein New Series IV/8G

96

2.1.3 Alkanols, C7

4-Heptanol (cont.) Table 2. Experimental values with uncertainties and deviation from calculated values. T K

ρexp ± 2σ est −3

kg ⋅ m

ρexp − ρcalc −3

kg ⋅ m

Ref. (Symbol in Fig. 1)

T K

ρexp ± 2σ est −3

kg ⋅ m

288.15 822.00 ± 1.00 −0.11 14-vav(✕ ) 293.15 817.20 ± 2.00 293.15 820.00 ± 2.00 1.49 19-beh(✕ ) 293.15 819.60 ± 2.00 290.85 819.30 ± 2.00 −0.88 19-eyk(✕ ) 303.05 811.40 ± 1.00 298.15 812.90 ± 0.30 −1.94 23-bru( ) 312.95 804.60 ± 1.00 298.15 815.60 ± 1.00 0.76 27-nor/cor(◆) 327.95 791.90 ± 1.00 295.15 817.00 ± 0.40 −0.05 30-err/she( ) 349.15 773.40 ± 1.00 273.15 833.50 ± 0.60 1.02 364.65 759.10 ± 1.00 30-she(∆) 288.15 821.90 ± 0.60 −0.21 381.45 742.90 ± 1.00 30-she(∆) 293.15 818.30 ± 0.60 −0.21 406.25 717.30 ± 1.00 30-she(∆) 293.15 820.00 ± 2.00 1.49 39-gol/tay(✕ ) 416.05 706.70 ± 1.00 Further references: [28-dil/luc, 36-tuo, 42-boe/han, 50-pic/zie].

kg ⋅ m

Ref. (Symbol in Fig. 1)

−1.31 1.09 0.22 1.02 0.37 −0.03 −0.29 −0.52 −1.09 −1.33

52-coo(✕ ) 56-shu/bel(✕ ) 63-tho/mea(∇) 63-tho/mea(∇) 63-tho/mea(∇) 63-tho/mea(∇) 63-tho/mea(∇) 63-tho/mea(∇) 63-tho/mea(∇) 63-tho/mea(∇)

−3

ρ

ρ

ρexp − ρcalc

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont. Landolt-Börnstein New Series IV/8G

2.1.3 Alkanols, C7

97

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ).

ρ ± σ fit kg ⋅ m−3

T K

834.58 ± 1.21 827.82 ± 1.15 820.79 ± 1.11 818.51 ± 1.10 814.84 ± 1.09 813.47 ± 1.09 805.87 ± 1.08

270.00 280.00 290.00 293.15 298.15 300.00 310.00

ρ ± σ fit kg ⋅ m−3

T K

797.99 ± 1.07 789.83 ± 1.07 781.39 ± 1.06 772.67 ± 1.05 763.67 ± 1.04 754.39 ± 1.02 744.83 ± 1.01

320.00 330.00 340.00 350.00 360.00 370.00 380.00

2-Methyl-1-hexanol

T K

[624-22-6]

390.00 400.00 410.00 420.00 430.00

ρ ± σ fit kg ⋅ m−3 734.99 ± 1.01 724.86 ± 1.02 714.46 ± 1.06 703.77 ± 1.13 692.81 ± 1.24

C7H16O

MW = 116.2

67

C7H16O

MW = 116.2

68

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 0.583. Coefficient ρ = A + BT 1054.84 A B −0.780 Table 2. Experimental values with uncertainties and deviation from calculated values. T K 286.15 293.15 293.15 293.15 1)

ρexp ± 2σ est

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−3

kg ⋅ m

831.3 ± 1.0 827.0 ± 1.0 825.7 ± 1.0 829.0 ± 2.0

−0.34 0.82 −0.48 2.82

08-zel/prz 08-zel/prz 50-pic/zie 54-naz/kak-11)

Not included in calculation of linear coefficients.

Table 3. Recommended values. T K 280.00 290.00

ρexp ± 2σ est −3

kg ⋅ m

836.4 ± 1.4 828.6 ± 0.9

2-Methyl-2-hexanol

T K 293.15 298.15

ρexp ± 2σ est kg ⋅ m−3

826.2 ± 0.9 822.3 ± 1.2 [625-23-0]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 4.8651 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.2332 · 10−1 (combined temperature ranges, unweighted). Coefficient A B C

T = 273.15 to 388.25 K ρ = A + BT + CT 2 + DT 3 + … 9.60129 · 102 −1.73590 · 10−1 −1.10338 · 10−3 cont.

Landolt-Börnstein New Series IV/8G

98

2.1.3 Alkanols, C7

2-Methyl-2-hexanol (cont.) Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

−3

kg ⋅ m

809.30 ± 1.00 814.60 ± 0.70 831.10 ± 1.00 809.70 ± 1.00 801.40 ± 1.00 792.90 ± 1.00 784.20 ± 1.00 776.00 ± 1.00 814.20 ± 0.50 813.60 ± 0.70 809.80 ± 0.60

−0.99 0.18 0.71 −0.59 −0.46 −0.32 −0.15 0.74 −0.22 −0.82 −0.49

kg ⋅ m

298.15 293.15 273.15 298.15 308.15 318.15 328.15 338.15 293.15 293.15 298.15

ρexp − ρcalc

−3

Ref. (Symbol in Fig. 1) 38-gin/hau(✕ ) 38-whi/ore(✕ ) 39-owe/qua( ) 39-owe/qua( ) 39-owe/qua( ) 39-owe/qua( ) 39-owe/qua( ) 39-owe/qua( ) 50-pic/zie( ) 52-lev/tan(◆) 53-sut(∇)

T K

293.15 293.15 293.15 293.15 303.05 311.95 327.75 349.05 364.75 380.55 388.25

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

814.60 ± 1.00 815.00 ± 1.00 815.00 ± 1.00 815.30 ± 1.00 806.40 ± 0.50 798.00 ± 0.50 785.20 ± 0.50 765.90 ± 0.50 749.80 ± 0.50 734.20 ± 0.55 726.00 ± 0.55

0.18 0.58 0.58 0.88 0.21 −0.60 0.49 0.79 −0.22 −0.08 −0.41

kg ⋅ m

Ref. (Symbol in Fig. 1) 54-naz/kak-2(✕ ) 54-naz/kak-2(✕ ) 57-pet/sus(✕ ) 59-pet/zak-1(✕ ) 63-tho/mea(∆) 63-tho/mea(∆) 63-tho/mea(∆) 63-tho/mea(∆) 63-tho/mea(∆) 63-tho/mea(∆) 63-tho/mea(∆)

ρ

ρ

Further references: [09-hen, 29-edg/cal, 33-whi/woo, 38-whi/joh].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont.

Landolt-Börnstein New Series IV/8G

2.1.3 Alkanols, C7

99

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ).

ρ ± σ fit kg ⋅ m−3

T K

832.82 ± 0.77 825.02 ± 0.77 816.99 ± 0.75 814.42 ± 0.74 810.29 ± 0.72 808.75 ± 0.71

270.00 280.00 290.00 293.15 298.15 300.00

ρ ± σ fit kg ⋅ m−3

T K

800.28 ± 0.66 791.59 ± 0.60 782.69 ± 0.54 773.56 ± 0.48 764.21 ± 0.45 754.64 ± 0.44

310.00 320.00 330.00 340.00 350.00 360.00

2-Methyl-3-hexanol

ρ ± σ fit kg ⋅ m−3

T K

744.85 ± 0.48 734.84 ± 0.59 724.60 ± 0.77 714.15 ± 1.04

370.00 380.00 390.00 400.00

[617-29-8]

C7H16O

MW = 116.2

69

Table 1. Fit with estimated B coefficient for 6 accepted points. Deviation σw = 0.661. Coefficient ρ = A + BT 1052.32 A B −0.780 Table 2. Experimental values with uncertainties and deviation from calculated values. T K

290.15 293.15 293.15 293.15 1)

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m

821.0 ± 6.0 825.0 ± 2.0 822.0 ± 2.0 822.8 ± 2.0

−5.01 1.33 −1.67 −0.87

ρexp ± 2σ est

T K

Ref.

kg ⋅ m−3

−3

Ref.

kg ⋅ m−3

kg ⋅ m

284.15 830.3 ± 2.0 293.15 823.9 ± 0.6 289.15 825.8 ± 2.0

06-mus1) 12-pic/ken 38-whi/joh 43-geo

ρexp − ρcalc

−3

−0.39 0.23 −0.99

48-mal/kon 50-pic/zie 54-naz/kak-1

Not included in calculation of linear coefficients.

Table 3. Recommended values. ρexp ± 2σ est

T K

T K

−3

kg ⋅ m

833.9 ± 1.9 826.1 ± 1.5

280.00 290.00

293.15 298.15

3-Methyl-1-hexanol

ρexp ± 2σ est kg ⋅ m−3

823.7 ± 1.5 819.8 ± 1.6

[13231-81-7]

C7H16O

MW = 116.2

Table 1. Experimental and recommended values with uncertainties. T K 293.15 298.15 302.15 1)

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

825.8 ± 1.0 824.5 ± 2.0 820.8 ± 2.0

24-dew/wec 27-nor/cor1) 31-lev/mar-51)

T K 297.15 293.15 293.15

Not included in calculation of recommended value.

Landolt-Börnstein New Series IV/8G

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

817.0 ± 5.0 825.8 ± 1.0 825.8 ± 1.0

41-hus/age1) 50-pic/zie Recommended

70

100

2.1.3 Alkanols, C7

3-Methyl-2-hexanol

[2313-65-7]

C7H16O

MW = 116.2

71

C7H16O

MW = 116.2

72

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

822.0 ± 0.8

12-bje-0

3-Methyl-3-hexanol

[597-96-6]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 8.4017 · 10−1 (combined temperature ranges, weighted), σc,uw = 2.5702 · 10−1 (combined temperature ranges, unweighted). T = 273.15 to 338.15 K ρ = A + BT + CT 2 + DT 3 + … 1.09518 · 103 −9.22352 · 10−1

Coefficient A B

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

296.75 288.15 293.15 298.15 273.15 298.15 308.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

819.90 ± 2.00 829.60 ± 1.00 825.40 ± 1.00 820.20 ± 1.00 841.50 ± 1.00 819.80 ± 1.00 810.70 ± 1.00

−1.57 0.20 0.61 0.02 −1.74 −0.38 −0.26

Ref. (Symbol in Fig. 1) 19-eyk(✕ ) 25-deg(∆) 25-deg(∆) 38-gin/hau(✕ ) 39-owe/qua(∇) 39-owe/qua(∇) 39-owe/qua(∇)

T K

318.15 328.15 338.15 290.15 293.15 293.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

801.60 ± 1.00 792.50 ± 1.00 783.50 ± 1.00 829.40 ± 1.00 825.40 ± 0.60 825.40 ± 0.60

−0.13 −0.01 0.21 1.84 0.61 0.61

Ref. (Symbol in Fig. 1) 39-owe/qua(∇) 39-owe/qua(∇) 39-owe/qua(∇) 46-shi(◆) 50-pic/zie( ) 55-soe/fre( )

Further references: [07-fou/tif, 14-hal, 29-edg/cal].

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15

ρ ± σ fit kg ⋅ m−3 846.14 ± 1.12 836.92 ± 1.06 827.70 ± 1.03 824.79 ± 1.02

T K

298.15 300.00 310.00 320.00

ρ ± σ fit kg ⋅ m−3 820.18 ± 1.01 818.47 ± 1.01 809.25 ± 1.03 800.03 ± 1.07

T K

330.00 340.00 350.00

ρ ± σ fit kg ⋅ m−3 790.80 ± 1.13 781.58 ± 1.20 772.36 ± 1.30

cont.

Landolt-Börnstein New Series IV/8G

101

ρ

ρ

2.1.3 Alkanols, C7

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

4-Methyl-1-hexanol

[818-49-5]

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 0.104. Coefficient ρ = A + BT 1052.63 A B −0.780 Table 2. Experimental values with uncertainties and deviation from calculated values. T K

293.15 297.15 293.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

823.9 ± 1.0 821.0 ± 1.0 823.9 ± 1.0

−0.07 0.15 −0.07

Table 3. Recommended values. T K 290.00 293.15 298.15

Landolt-Börnstein New Series IV/8G

ρexp ± 2σ est kg ⋅ m−3

826.4 ± 0.9 824.0 ± 0.9 820.1 ± 0.9

Ref. 24-dew/wec 41-hus/age 50-pic/zie

C7H16O

MW = 116.2

73

102

2.1.3 Alkanols, C7

4-Methyl-2-hexanol

[2313-61-3]

C7H16O

MW = 116.2

74

C7H16O

MW = 116.2

75

C7H16O

MW = 116.2

76

Table 1. Experimental values with uncertainties. T K

298.15 295.15 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

817.7 ± 2.0 816.0 ± 2.0 810.0 ± 8.0

30-dav/dix 31-lev/mar-4 53-ner/hen

5-Methyl-1-hexanol

[627-98-5]

Table 1. Experimental and recommended values with uncertainties. T K 298.15 297.15 293.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

kg ⋅ m−3

819.2 ± 6.0 819.0 ± 5.0 822.6 ± 3.0 815.7 ± 1.0 815.7 ± 1.0

16-lev/all1) 41-hus/age1) 54-naz/kak-21) 52-coo Recommended

Not included in calculation of recommended value.

5-Methyl-2-hexanol

[627-59-8]

Table 1. Fit with estimated B coefficient for 4 accepted points. Deviation σw = 1.301. Coefficient ρ = A + BT 1049.27 A B −0.800 Table 2. Experimental values with uncertainties and deviation from calculated values. T K

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

290.65 818.5 ± 2.0 290.65 817.4 ± 2.0 293.15 813.1 ± 2.0 1)

1.75 0.65 −1.65

Ref. 1878-roh 1878-roh 36-tuo

T K

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

293.15 814.0 ± 2.0 277.15 822.0 ± 4.0

−0.75 −5.55

Ref. 38-whi/joh 49-mal/vol1)

Not included in calculation of linear coefficients.

Table 3. Recommended values. T K 290.00 293.15 298.15

ρexp ± 2σ est kg ⋅ m−3

817.3 ± 1.9 814.7 ± 1.9 810.7 ± 2.0

Landolt-Börnstein New Series IV/8G

2.1.3 Alkanols, C7 5-Methyl-3-hexanol

[623-55-2]

103 C7H16O

MW = 116.2

77

C7H16O

MW = 116.2

78

C7H16O

MW = 116.2

79

C7H16O

MW = 116.2

80

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

833.1 ± 1.0

57-shu/bel

2,2,3-Trimethyl-1-butanol

[55505-23-2]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

kg ⋅ m−3

846.6 ± 1.0

41-gle

2,3,3-Trimethyl-1-butanol

[36794-64-6]

Table 1. Experimental values with uncertainties. ρexp ± 2σ est

T K

298.15 293.15

Ref.

kg ⋅ m−3

823.8 ± 2.0 837.2 ± 2.0

56-sar/new 66-far/per

2,3,3-Trimethyl-2-butanol

[594-83-2]

Table 1. Fit with estimated B coefficient for 4 accepted points. Deviation σw = 0.081. Coefficient ρ = A + BT 1116.79 A B −0.950 Table 2. Experimental values with uncertainties and deviation from calculated values. T K 298.15 298.15 293.15 1)

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

838.0 ± 3.0 833.5 ± 0.5 838.2 ± 0.5

4.46 −0.03 −0.07

Ref. 38-gin/hau1) 85-wie/sip 88-sip/wie

Not included in calculation of linear coefficients.

Table 3. Recommended values. T K

290.00 293.15 298.15 310.00

Landolt-Börnstein New Series IV/8G

ρexp ± 2σ est kg ⋅ m−3

841.3 ± 0.5 838.3 ± 0.4 833.5 ± 0.3 822.3 ± 0.7

T K 298.15 303.15 308.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

833.5 ± 0.5 828.9 ± 0.5 819.2 ± 2.0

−0.03 0.14 −4.87

Ref. 88-sip/wie 88-sip/wie 88-sip/wie1)

2.1.4 Alkanols, C8

105

2.1.4 Alkanols, C8 3,3-Dimethyl-2-ethyl-1-butanol

[66576-56-5]

C8H18O

MW = 130.23

81

C8H18O

MW = 130.23

82

C8H18O

MW = 130.23

83

C8H18O

MW = 130.23

84

C8H18O

MW = 130.23

85

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

842.5 ± 1.0

56-sar/new

2,2-Dimethyl-1-hexanol

[2370-13-0]

Table 1. Experimental values with uncertainties. T K 293.15 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

826.5 ± 2.0 839.8 ± 2.0

64-blo/hag 65-shu/puz

2,2-Dimethyl-3-hexanol

[4209-90-9]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est

T K

290.15 293.15 293.15 1)

Ref.

kg ⋅ m−3

830.0 ± 5.0 834.2 ± 2.0 834.2 ± 2.0

21-ler1) 44-hen/mat Recommended

Not included in calculation of recommended value.

2,3-Dimethyl-2-hexanol

[19550-03-9]

Table 1. Experimental and recommended values with uncertainties. T K 298.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

kg ⋅ m−3

831.0 ± 2.0 836.5 ± 1.0 836.5 ± 1.0

43-ste/gre1) 41-hus/gui Recommended

Not included in calculation of recommended value.

2,3-Dimethyl-3-hexanol

[4166-46-5]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

837.1 ± 2.0

Landolt-Börnstein New Series IV/8G

26-sta

106

2.1.4 Alkanols, C8

2,4-Dimethyl-2-hexanol

[42328-76-7

C8H18O

MW = 130.23

86

C8H18O

MW = 130.23

87

Table 1. Experimental and recommended values with uncertainties. T K

294.15 293.15 301.15 301.15 1)

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

827.0 ± 10.0 809.9 ± 2.0 806.5 ± 1.0 806.5 ± 1.0

31-lev/mar-21) 41-hus/gui1) 60-tha/vas Recommended

Not included in calculation of recommended value.

2,5-Dimethyl-1-hexanol

[6886-16-4]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 1.3629 · 10−1 (combined temperature ranges, weighted), σc,uw = 3.8771 · 10−2 (combined temperature ranges, unweighted). T = 273.15 to 373.15 K ρ = A + BT + CT 2 + DT 3 + … 9.26323 · 102 −1.60894 · 10−3 −1.13959 · 10−3

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

273.15 285.15 293.15 303.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

841.00 ± 1.50 833.00 ± 1.50 828.00 ± 1.50 821.00 ± 1.50

0.14 −0.20 0.08 −0.11

Ref. (Symbol in Fig. 1) 1879-car( 1879-car( 1879-car( 1879-car(

) ) ) )

T K

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

313.15 814.00 ± 1.50 323.15 807.00 ± 1.50 373.15 767.00 ± 2.00

−0.07 0.20 −0.05

Ref. (Symbol in Fig. 1)

1879-car( ) 1879-car( ) 1879-car( )

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15

ρ ± σ fit kg ⋅ m−3 842.81 ± 1.75 836.53 ± 1.59 830.02 ± 1.53 827.92 ± 1.53 824.54 ± 1.53

T K

300.00 310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 823.28 ± 1.53 816.31 ± 1.55 809.11 ± 1.58 801.69 ± 1.62 794.04 ± 1.67

T K

350.00 360.00 370.00 380.00

ρ ± σ fit kg ⋅ m−3 786.16 ± 1.77 778.05 ± 1.95 769.72 ± 2.23 761.15 ± 2.64

cont.

Landolt-Börnstein New Series IV/8G

107

ρ

ρ

2.1.4 Alkanols, C8

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

2,5-Dimethyl-2-hexanol

[3730-60-7]

C8H18O

MW = 130.23

88

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.390. ρ = A + BT Coefficient 1044.07 A B −0.780

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 293.15 293.15 293.15 302.15 1)

ρexp ± 2σ est −3

kg ⋅ m

822.8 ± 5.0 810.5 ± 3.0 815.8 ± 1.0 808.0 ± 1.0

ρexp − ρcalc

Ref.

−3

kg ⋅ m

7.39 −4.91 0.39 −0.39

02-kon1) 33-mey/tuo1) 41-hus/gui 56-woo/vio

Not included in calculation of linear coefficients.

cont. Landolt-Börnstein New Series IV/8G

108

2.1.4 Alkanols, C8

2,5-Dimethyl-2-hexanol (cont.) Table 3. Recommended values. ρexp ± 2σ est

T K

kg ⋅ m−3

817.9 ± 0.7 815.4 ± 0.6 811.5 ± 0.6 802.3 ± 0.9

290.00 293.15 298.15 310.00

2,5-Dimethyl-3-hexanol

[19550-07-3]

C8H18O

MW = 130.23

89

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 8.1519 · 10−1 (combined temperature ranges, weighted), σc,uw = 3.4359 · 10−1 (combined temperature ranges, unweighted). T = 273.15 to 323.15 K ρ = A + BT + CT 2 + DT 3 + … 8.97260 · 102 2.17973 · 10−1 −1.67297 · 10−3

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 288.15 293.15 298.15 303.15 313.15 323.15 288.15 1)

ρexp ± 2σ est

ρexp − ρcalc

−3

kg ⋅ m

Ref. (Symbol in Fig. 1)

820.00 ± 1.50 817.00 ± 2.00 814.00 ± 2.00 811.00 ± 1.50 801.00 ± 2.00 793.00 ± 2.00 820.00 ± 1.50

−1.16 −0.39 0.47 1.41 −0.46 0.00 −1.16

1879-car(∆) 1879-car(∆) 1879-car(∆) 1879-car(∆) 1879-car(∆) 1879-car(∆) 00-car-1( )

kg ⋅ m

−3

T K 303.15 313.15 323.15 273.15 293.15 293.15 293.15

ρexp ± 2σ est

ρexp − ρcalc

−3

kg ⋅ m

Ref. (Symbol in Fig. 1)

811.00 ± 1.50 801.00 ± 2.00 793.00 ± 2.00 832.40 ± 1.00 822.10 ± 4.00 819.50 ± 2.00 815.20 ± 3.00

1.41 −0.46 0.00 0.42 4.71 2.11 −2.19

00-car-1( ) 00-car-1( ) 00-car-1( ) 13-fav( ) 13-fav1) 43-geo(∇) 53-sok(◆)

−3

kg ⋅ m

Not included in Fig. 1.

Further references: [12-mic, 36-tuo, 48-mal/kon]. Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00

ρ ± σ fit kg ⋅ m−3 834.15 ± 2.07 827.13 ± 2.05 819.78 ± 2.03

T K

293.15 298.15 300.00

ρ ± σ fit kg ⋅ m−3 817.39 ± 1.99 813.53 ± 1.97 812.08 ± 1.96

T K

310.00 320.00 330.00

ρ ± σ fit kg ⋅ m−3 804.06 ± 1.86 795.70 ± 2.10 787.00 ± 3.06 cont. Landolt-Börnstein New Series IV/8G

109

ρ

ρ

2.1.4 Alkanols, C8

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

3,3-Dimethyl-1-hexanol

[10524-70-6]

C8H18O

MW = 130.23

90

C8H18O

MW = 130.23

91

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

kg ⋅ m−3

839.0 ± 2.0

64-sta-1

3,3-Dimethyl-2-hexanol

[22025-20-3]

Table 1. Experimental and recommended values with uncertainties. T K 293.15 273.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

kg ⋅ m−3

845.7 ± 1.0 880.8 ± 10. 845.9 ± 1.0 845.9 ± 1.0

57-bol/ego-1 57-bol/ego-11) 58-ego Recommended

Not included in calculation of recommended value.

Landolt-Börnstein New Series IV/8G

110

2.1.4 Alkanols, C8

3,4-Dimethyl-3-hexanol

[19550-08-4]

C8H18O

MW = 130.23

92

C8H18O

MW = 130.23

93

C8H18O

MW = 130.23

94

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

834.5 ± 2.0

48-hus/goe

3,5-Dimethyl-1-hexanol

[13501-73-0]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

828.2 ± 2.0

59-hos/nis

3,5-Dimethyl-3-hexanol

[4209-91-0]

Table 2. Experimental and recommended values with uncertainties. T K

288.15 293.15 288.15 298.15 293.15 1)

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

830.0 ± 3.0 822.8 ± 3.0 830.0 ± 3.0 827.0 ± 3.0 828.8 ± 2.0

09-bod/tab1) 33-mey/tuo1) 50-doe/zei1) 56-woo/vio1) 58-pan/osi

T K

293.15 293.15 293.15 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

826.1 ± 2.0 826.1 ± 2.0 827.2 ± 2.0 827.0 ± 2.0

59-pet/zak 59-pet/zak-1 61-sok/she Recommended

Not included in calculation of recommended value.

4,4-Dimethyl-3-hexanol

[19550-09-5]

C8H18O

MW = 130.23

95

C8H18O

MW = 130.23

96

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

834.1 ± 2.0

51-lev/fai

5,5-Dimethyl-3-hexanol

[66576-31-6]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

833.9 ± 1.0

41-whi/whi

Landolt-Börnstein New Series IV/8G

2.1.4 Alkanols, C8 2-Ethyl-1-hexanol

[104-76-7]

111 C8H18O

MW = 130.23

97

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 8.7629 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.8894 · 10−1 (combined temperature ranges, unweighted). T = 273.15 to 373.64 K ρ = A + BT + CT 2 + DT 3 + … 1.00464 · 103 −4.24121 · 10−1 −5.58140 · 10−4

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 273.15 273.19 283.15 293.15 303.15 313.15 333.15 353.15 373.64 298.15 292.15 293.15 310.15 317.15 367.15 1)

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

848.30 ± 2.00 846.38 ± 1.00 838.93 ± 1.00 831.60 ± 1.00 824.13 ± 1.00 816.79 ± 1.00 801.15 ± 1.00 785.61 ± 1.00 768.40 ± 1.00 829.30 ± 1.00 834.20 ± 2.00 833.40 ± 2.00 820.50 ± 2.00 815.00 ± 2.00 777.00 ± 2.00

1.15 −0.74 −0.87 −0.74 −0.64 −0.30 −0.25 0.36 0.15 0.73 1.11 1.06 1.09 1.01 3.31

T K 01-gue-1(✕ ) 293.15 30-bin/dar(✕ ) 293.15 30-bin/dar(✕ ) 293.15 30-bin/dar1) 293.15 30-bin/dar(✕ ) 293.15 30-bin/dar(✕ ) 298.15 30-bin/dar(✕ ) 303.15 30-bin/dar(✕ ) 308.15 30-bin/dar(✕ ) 313.15 36-lev/rot-1(✕ ) 318.15 39-ken/pla1) 323.15 39-ken/pla1) 328.15 39-ken/pla(✕ ) 333.15 39-ken/pla(✕ ) 298.15 39-ken/pla1)

Ref. (Symbol in Fig. 1)

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

0.26 832.60 ± 0.40 0.16 832.50 ± 0.50 0.26 832.60 ± 0.40 0.26 832.60 ± 0.50 832.10 ± 1.00 −0.24 827.50 ± 1.00 −1.07 823.10 ± 1.00 −1.67 818.50 ± 0.00 −2.45 812.40 ± 0.00 −4.69 807.30 ± 0.00 −5.91 801.80 ± 0.00 −7.50 795.20 ± 0.00 −10.16 790.70 ± 0.00 −10.70 0.13 828.70 ± 0.50

Ref. (Symbol in Fig. 1)

56-ano-1( ) 58-ano-5(∆) 61-dyk/sep( ) 68-ano(◆) 85-chi/lin1) 85-chi/lin(✕ ) 85-chi/lin(✕ ) 85-chi/lin1) 85-chi/lin1) 85-chi/lin1) 85-chi/lin1) 85-chi/lin1) 85-chi/lin1) 88-cab/bar(∇)

Not included in Fig. 1.

Further references: [22-lev/tay-1, 34-von/man, 37-mas, 38-mas, 39-gol/tay, 51-hau, 58-kut/lyu, 58-lyu, 58-lyu/bel, 60-tje, 63-lyu/mer]. Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15

ρ ± σ fit kg ⋅ m−3 849.44 ± 1.21 842.13 ± 1.06 834.70 ± 1.01 832.34 ± 1.01 828.57 ± 1.01

T K

300.00 310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 827.17 ± 1.02 819.52 ± 1.05 811.77 ± 1.09 803.90 ± 1.11 795.92 ± 1.13

T K

350.00 360.00 370.00 380.00

ρ ± σ fit kg ⋅ m−3 787.82 ± 1.15 779.62 ± 1.19 771.30 ± 1.29 762.88 ± 1.48

cont.

Landolt-Börnstein New Series IV/8G

112

2.1.4 Alkanols, C8

ρ

ρ

2-Ethyl-1-hexanol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

3-Ethyl-1-hexanol

[41065-95-6]

C8H18O

MW = 130.23

98

C8H18O

MW = 130.23

99

Table 1. Experimental value with uncertainty. T K 301.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

829.0 ± 3.0

3-Ethyl-3-hexanol

31-lev/mar-3 [597-76-2]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 8.6240 · 10−1 (combined temperature ranges, weighted), σc,uw = 4.3902 · 10−1 (combined temperature ranges, unweighted). Coefficient A B C

T = 273.15 to 338.15 K ρ = A + BT + CT 2 + DT 3 + … 8.03283 · 102 1.10512 −3.35884 · 10−3 cont.

Landolt-Börnstein New Series IV/8G

2.1.4 Alkanols, C8

113

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

−3

kg ⋅ m

836.50 ± 1.00 843.40 ± 2.00 837.30 ± 2.00 854.60 ± 1.00 833.30 ± 1.00

−0.36 0.52 −1.30 0.06 −0.90

kg ⋅ m

Ref. (Symbol in Fig. 1)

T K

308.15 14-hal(∆) 19-eyk(◆) 318.15 328.15 22-bae(∇) 39-owe/qua( ) 338.15 39-owe/qua( ) 293.15

ρexp ± 2σ est

ρexp − ρcalc kg ⋅ m−3

−3

kg ⋅ m

824.60 ± 1.00 815.60 ± 1.00 806.70 ± 1.00 790.80 ± 1.00 839.80 ± 1.00

−0.28 0.70 2.46 −2.11 1.20

Ref. (Symbol in Fig. 1)

) ) ) )

39-owe/qua( 39-owe/qua( 39-owe/qua( 39-owe/qua( 55-ano( )

ρ

ρ

295.15 288.10 293.15 273.15 298.15

ρexp − ρcalc

−3

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15

Landolt-Börnstein New Series IV/8G

ρ ± σ fit kg ⋅ m−3 856.81 ± 1.42 849.38 ± 1.40 841.29 ± 1.34 838.60 ± 1.34

T K

298.15 300.00 310.00 320.00

ρ ± σ fit kg ⋅ m−3 834.20 ± 1.28 832.52 ± 1.25 823.09 ± 1.02 812.98 ± 0.83

T K

330.00 340.00 350.00

ρ ± σ fit kg ⋅ m−3 802.19 ± 0.94 790.74 ± 1.50 778.62 ± 2.63

114

2.1.4 Alkanols, C8

4-Ethyl-3-hexanol

[19780-44-0]

C8H18O

MW = 130.23

100

C8H18O

MW = 130.23

101

C8H18O

MW = 130.23

102

C8H18O

MW = 130.23

103

Table 1. Experimental value with uncertainty. T K 273.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

835.0 ± 3.0

07-fou/tif

2-Ethyl-4-methyl-1-pentanol

[106-67-2]

Table 1. Experimental values with uncertainties. T K 293.15 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

830.0 ± 2.0 827.3 ± 0.6

58-ano-3 61-dyk/sep

3-Ethyl-2-methyl-2-pentanol

[19780-63-3]

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.150. Coefficient ρ = A + BT 1067.01 A B −0.780 Table 2. Experimental values with uncertainties and deviation from calculated values. T K

293.15 298.15

ρexp ± 2σ est −3

kg ⋅ m

838.2 ± 1.0 834.6 ± 1.

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−0.15 0.15

41-hus/gui 54-ski/flo

Table 3. Recommended values. T K

290.00 293.15 298.15

ρexp ± 2σ est kg ⋅ m−3

840.8 ± 0.9 838.4 ± 0.9 834.5 ± 0.9

3-Ethyl-2-methyl-3-pentanol

[597-05-7]

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.200. Coefficient ρ = A + BT 1070.08 A B −0.820 cont.

Landolt-Börnstein New Series IV/8G

2.1.4 Alkanols, C8

115

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 273.15 293.15

ρexp ± 2σ est

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−3

kg ⋅ m

846.3 ± 2.0 829.5 ± 2.0

0.20 −0.20

1891-gri/paw 1891-gri/paw

Table 3. Recommended values. ρexp ± 2σ est

T K 270.00 280.00 290.00 293.15 298.15

kg ⋅ m−3

848.7 ± 2.2 840.5 ± 1.8 832.3 ± 1.9 829.7 ± 2.1 825.6 ± 2.3

3-Ethyl-3-methyl-2-pentanol

[66576-22-5]

C8H18O

MW = 130.23

104

C8H18O

MW = 130.23

105

Table 1. Experimental values with uncertainties. ρexp ± 2σ est

T K

293.15 293.15

Ref.

−3

kg ⋅ m

857.6 ± 1.0 857.6 ± 1.0

57-bol/ego 58-ego

2-Methyl-1-heptanol

[60435-70-3]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 2.1063 · 10−1 (combined temperature ranges, weighted), σc,uw = 9.7608 · 10−2 (combined temperature ranges, unweighted). T = 273.15 to 372.82 K ρ = A + BT + CT 2 + DT 3 + … 9.49326 · 102 −2.66559 · 10−1 −8.01222 · 10−4

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

273.23 283.15 293.15 303.15 313.15 333.15 1)

ρexp ± 2σ est −3

kg ⋅ m

816.93 ± 1.00 809.19 ± 1.00 801.99 ± 1.00 795.42 ± 1.00 787.03 ± 1.00 771.49 ± 1.00

ρexp − ρcalc kg ⋅ m−3

0.25 −0.42 −0.34 0.53 −0.25 −0.11

Ref. (Symbol in Fig. 1)

) ) ) ) ) )

30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar(

T K

353.15 372.82 273.15 293.15 298.15

ρexp ± 2σ est −3

kg ⋅ m

755.69 ± 1.00 738.39 ± 1.00 816.80 ± 0.60 802.30 ± 0.60 798.70 ± 0.60

ρexp − ρcalc kg ⋅ m−3

0.42 −0.19 0.06 −0.03 0.07

Ref. (Symbol in Fig. 1)

) ) ) ) )

30-bin/dar( 30-bin/dar( 41-dor/gla( 41-dor/gla( 41-dor/gla(

Not included in Fig. 1.

cont.

Landolt-Börnstein New Series IV/8G

116

2.1.4 Alkanols, C8

ρ

ρ

2-Methyl-1-heptanol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15

ρ ± σ fit kg ⋅ m−3 818.95 ± 0.95 811.87 ± 0.87 804.64 ± 0.87 802.33 ± 0.87 798.63 ± 0.89

T K

300.00 310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 797.25 ± 0.90 789.70 ± 0.94 781.98 ± 0.98 774.11 ± 1.00 766.07 ± 1.02

T K

350.00 360.00 370.00 380.00

ρ ± σ fit kg ⋅ m−3 757.88 ± 1.05 749.53 ± 1.12 741.01 ± 1.25 732.34 ± 1.45

Landolt-Börnstein New Series IV/8G

2.1.4 Alkanols, C8 2-Methyl-2-heptanol

[625-25-2]

117 C8H18O

MW = 130.23

106

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 7.1719 · 10−1 (combined temperature ranges, weighted), σc,uw = 2.6066 · 10−1 (combined temperature ranges, unweighted). Coefficient A B C

T = 273.15 to 372.77 K ρ = A + BT + CT 2 + DT 3 + … 9.54283 · 102 −1.78842 · 10−1 −1.09478 · 10−3

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

822.98 ± 1.00 814.66 ± 1.00 807.30 ± 1.00 798.91 ± 1.00 790.76 ± 1.00

−0.74 −1.21 −0.47 −0.55 −0.16

Ref. (Symbol in Fig. 1)

) ) ) ) )

30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar(

T K

333.15 353.15 372.77 273.15 298.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

Ref. (Symbol in Fig. 1)

0.09 0.58 0.35 0.75 1.36

30-bin/dar( 30-bin/dar( 30-bin/dar( 41-dor/gla( 41-dor/gla(

773.28 ± 1.00 755.17 ± 1.00 735.84 ± 1.00 824.50 ± 0.60 805.00 ± 0.60

) ) ) ) )

ρ

ρ

273.19 283.15 293.15 303.15 313.15

ρexp ± 2σ est

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont. Landolt-Börnstein New Series IV/8G

118

2.1.4 Alkanols, C8

2-Methyl-2-heptanol (cont.) Further references: [06-mus, 33-whi/wil, 41-hus/gui, 44-qua/sma, 57-col/fal]. Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ).

ρ ± σ fit kg ⋅ m−3

T K

T K

826.19 ± 0.99 818.38 ± 0.91 810.35 ± 0.90 807.77 ± 0.91 803.64 ± 0.93

270.00 280.00 290.00 293.15 298.15

300.00 310.00 320.00 330.00 340.00

2-Methyl-3-heptanol

ρ ± σ fit kg ⋅ m−3

T K

802.10 ± 0.93 793.63 ± 0.97 784.95 ± 1.00 776.04 ± 1.02 766.92 ± 1.03

[18720-62-2]

350.00 360.00 370.00 380.00

C8H18O

ρ ± σ fit kg ⋅ m−3 757.58 ± 1.06 748.02 ± 1.12 738.24 ± 1.25 728.24 ± 1.47

MW = 130.23

107

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 2.3940 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.0583 · 10−1 (combined temperature ranges, unweighted). T = 273.15 to 373.52 K ρ = A + BT + CT 2 + DT 3 + …

Coefficient A B C

9.51750 · 102 −8.19206 · 10−2 −1.19870 · 10−3

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 293.15 293.15 298.15 273.21 283.15 293.15 303.15 313.15

ρexp ± 2σ est

ρexp − ρcalc kg ⋅ m

Ref. (Symbol in Fig. 1)

0.28 −1.22 0.23 0.30 −0.36 −0.05 −0.10 0.18

06-mus(✕ ) 12-pic/ken(∆) 13-tho(✕ ) 30-bin/dar(◆) 30-bin/dar(◆) 30-bin/dar(◆) 30-bin/dar(◆) 30-bin/dar(◆)

−3

−3

kg ⋅ m

825.00 ± 1.00 823.50 ± 1.00 821.00 ± 1.00 840.19 ± 1.00 832.09 ± 1.00 824.67 ± 1.00 816.66 ± 1.00 808.73 ± 1.00

T K 333.15 353.15 373.52 273.15 298.15 293.15 284.15

ρexp ± 2σ est

ρexp − ρcalc kg ⋅ m

Ref. (Symbol in Fig. 1)

−0.16 0.25 0.07 0.06 0.23 0.38 −0.09

30-bin/dar(◆) 30-bin/dar(◆) 30-bin/dar(◆) 41-dor/gla( ) 41-dor/gla( ) 43-geo(∇) 48-mal/kon( )

−3

−3

kg ⋅ m

791.26 ± 1.00 773.57 ± 1.00 753.98 ± 1.00 840.00 ± 0.60 821.00 ± 0.60 825.10 ± 1.00 831.60 ± 1.00

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K 270.00 280.00 290.00 293.15 298.15

ρ ± σ fit kg ⋅ m−3 842.25 ± 1.31 834.83 ± 1.34 827.18 ± 1.30 824.72 ± 1.28 820.77 ± 1.23

T K 300.00 310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 819.29 ± 1.21 811.16 ± 1.09 802.79 ± 0.98 794.18 ± 0.91 785.33 ± 0.93

T K 350.00 360.00 370.00 380.00

ρ ± σ fit kg ⋅ m−3 776.24 ± 1.10 766.91 ± 1.46 757.34 ± 2.04 747.53 ± 2.85

cont. Landolt-Börnstein New Series IV/8G

2.1.4 Alkanols, C8

119

ρ

ρ

Further references: [14-wal-1, 33-bri, 36-tuo].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

2-Methyl-4-heptanol

[21570-35-4]

C8H18O

MW = 130.23

108

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 1.1397 · 10−1 (combined temperature ranges, weighted), σc,uw = 5.7770 · 10−2 (combined temperature ranges, unweighted). Coefficient A B C

T = 273.15 to 373.54 K ρ = A + BT + CT 2 + DT 3 + … 9.33558 · 102 −7.11104 · 10−2 −1.15359 · 10−3

cont. Landolt-Börnstein New Series IV/8G

120

2.1.4 Alkanols, C8

2-Methyl-4-heptanol (cont.) Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

−3

kg ⋅ m

828.36 ± 1.00 820.75 ± 1.00 813.47 ± 1.00 805.80 ± 1.00 798.28 ± 1.00 781.86 ± 1.00

0.35 −0.19 −0.11 −0.19 0.11 0.03

kg ⋅ m

273.23 283.15 293.15 303.15 313.15 333.15

ρexp − ρcalc

−3

Ref. (Symbol in Fig. 1)

) ) ) ) ) )

30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar(

ρexp ± 2σ est

T K

353.15 373.54 273.15 293.15 298.15

ρexp − ρcalc −3

−3

kg ⋅ m

764.82 ± 1.00 745.82 ± 1.00 828.10 ± 0.60 813.50 ± 0.60 809.80 ± 0.60

0.24 −0.21 0.04 −0.08 −0.01

kg ⋅ m

Ref. (Symbol in Fig. 1)

) ) ) ) )

30-bin/dar( 30-bin/dar( 41-dor/gla( 41-dor/gla( 41-dor/gla(

ρ

ρ

Further references: [06-mus, 36-tuo, 57-shu/bel].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15

ρ ± σ fit kg ⋅ m−3 830.26 ± 1.23 823.21 ± 0.99 815.92 ± 0.88 813.58 ± 0.87 809.81 ± 0.87

T K

300.00 310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 808.40 ± 0.87 800.65 ± 0.91 792.68 ± 0.98 784.47 ± 1.04 776.03 ± 1.09

T K

350.00 360.00 370.00 380.00

ρ ± σ fit kg ⋅ m−3 767.35 ± 1.13 758.45 ± 1.17 749.32 ± 1.22 739.96 ± 1.32

Landolt-Börnstein New Series IV/8G

2.1.4 Alkanols, C8 3-Methyl-1-heptanol

[1070-32-2]

121 C8H18O

MW = 130.23

109

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 7.0802 · 10−2 (combined temperature ranges, weighted), σc,uw = 3.3702 · 10−2 (combined temperature ranges, unweighted). Coefficient A B C

T = 273.15 to 373.62 K ρ = A + BT + CT 2 + DT 3 + … 9.62326 · 102 −4.50758 · 10−1 −4.89103 · 10−4

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

802.83 ± 1.00 795.29 ± 1.00 788.15 ± 1.00 780.64 ± 1.00 773.34 ± 1.00

0.15 −0.19 −0.00 −0.09 0.13

Ref. (Symbol in Fig. 1)

) ) ) ) )

30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar(

T K 333.15 353.15 373.62 273.15 298.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

757.81 ± 1.00 742.17 ± 1.00 725.64 ± 1.00 802.70 ± 0.60 784.50 ± 0.60

−0.06 0.03 0.00 −0.01 0.05

Ref. (Symbol in Fig. 1)

) ) ) ) )

30-bin/dar( 30-bin/dar( 30-bin/dar( 41-dor/gla( 41-dor/gla(

ρ

ρ

T K 273.19 283.15 293.15 303.15 313.15

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont.

Landolt-Börnstein New Series IV/8G

122

2.1.4 Alkanols, C8

3-Methyl-1-heptanol (cont.) Further references: [31-lev/mar-5, 33-bri, 41-hus/age, 56-lic/dur].

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15

ρ ± σ fit kg ⋅ m−3

ρ ± σ fit kg ⋅ m−3

T K

804.97 ± 0.99 797.77 ± 0.91 790.47 ± 0.90 788.15 ± 0.91 784.45 ± 0.93

783.08 ± 0.93 775.59 ± 0.97 768.00 ± 1.00 760.31 ± 1.02 752.53 ± 1.03

300.00 310.00 320.00 330.00 340.00

3-Methyl-2-heptanol

[31367-46-1]

ρ ± σ fit kg ⋅ m−3

T K

350.00 360.00 370.00 380.00

C8H18O

744.65 ± 1.06 736.67 ± 1.12 728.59 ± 1.24 720.41 ± 1.45

MW = 130.23

110

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 0.094. Coefficient ρ = A + BT 1056.15 A B −0.800

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 286.15 273.15 298.15 293.15 283.15 293.15 1)

ρexp ± 2σ est

ρexp − ρcalc

−3

kg ⋅ m

Ref.

−3

kg ⋅ m

827.2 ± 2.00 −0.03 837.5 ± 1.00 −0.13 0.07 817.7 ± 1.00 0.07 821.7 ± 1.00 797.6 ± 10.00 −32.05 790.0 ± 10.00 −31.62

24-pow1) 41-dor/gla 41-dor/gla 41-dor/gla 30-bin/dar1) 30-bin/dar1)

T K 303.15 313.15 333.15 353.15 373.44 273.20

ρexp ± 2σ est −3

kg ⋅ m

781.5 ± 10.00 773.7 ± 10.00 756.0 ± 10.00 738.4 ± 10.00 723.5 ± 10.00 806.3 ± 10.00

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−32.14 −31.88 −33.60 −35.19 −33.92 −31.27

30-bin/dar1) 30-bin/dar1) 30-bin/dar1) 30-bin/dar1) 30-bin/dar1) 30-bin/dar1)

Not included in calculation of linear coefficients.

Table 3. Recommended values. T K 270.00 280.00 290.00 293.15 298.15

ρexp ± 2σ est kg ⋅ m−3

840.2 ± 0.9 832.2 ± 0.5 824.2 ± 0.3 821.6 ± 0.3 817.6 ± 0.6

Landolt-Börnstein New Series IV/8G

2.1.4 Alkanols, C8 3-Methyl-3-heptanol

[5582-82-1]

123 C8H18O

MW = 130.23

111

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 9.7126 · 10−1 (combined temperature ranges, weighted), σc,uw = 2.4649 · 10−1 (combined temperature ranges, unweighted). T = 273.15 to 373.54 K ρ = A + BT + CT 2 + DT 3 + … 1.00165 · 103 −3.47181 · 10−1 −8.23886 · 10−4

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 273.23 283.15 293.15 303.15 313.15 333.15 353.15 373.54 273.15 288.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

845.31 ± 1.00 837.17 ± 1.00 829.19 ± 1.00 821.02 ± 1.00 812.61 ± 1.00 794.47 ± 1.00 776.10 ± 1.00 757.17 ± 1.00 844.60 ± 2.00 832.50 ± 2.00

0.03 −0.12 0.12 0.33 0.47 −0.07 −0.19 0.17 −0.75 −0.70

Ref. (Symbol in Fig. 1) 30-bin/dar(∆) 30-bin/dar(∆) 30-bin/dar(∆) 30-bin/dar(∆) 30-bin/dar(∆) 30-bin/dar(∆) 30-bin/dar(∆) 30-bin/dar(∆) 30-van(◆) 30-van(◆)

T K 293.15 298.15 273.15 298.15 298.15 318.15 328.15 298.15 293.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

828.20 ± 2.00 824.90 ± 2.00 847.10 ± 1.00 827.10 ± 1.00 825.20 ± 1.00 808.30 ± 1.00 799.90 ± 1.00 823.00 ± 2.00 826.90 ± 1.00

−0.87 0.00 1.75 2.20 0.30 0.50 0.90 −1.90 −2.17

Ref. (Symbol in Fig. 1) 33-whi/woo(✕ ) 33-whi/woo(✕ ) 41-dor/gla(∇) 41-dor/gla(∇) 44-qua/sma( ) 44-qua/sma( ) 44-qua/sma( ) 61-wib/fos(✕ ) 66-are/tav( )

Further references: [02-kon, 65-col/des].

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15

ρ ± σ fit kg ⋅ m−3 847.85 ± 1.56 839.85 ± 1.43 831.68 ± 1.35 829.07 ± 1.33 824.90 ± 1.31

T K

300.00 310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 823.35 ± 1.30 814.85 ± 1.26 806.19 ± 1.22 797.36 ± 1.17 788.37 ± 1.13

T K

350.00 360.00 370.00 380.00

ρ ± σ fit kg ⋅ m−3 779.21 ± 1.09 769.89 ± 1.10 760.40 ± 1.18 750.75 ± 1.35

cont.

Landolt-Börnstein New Series IV/8G

124

2.1.4 Alkanols, C8

ρ

ρ

3-Methyl-3-heptanol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

3-Methyl-4-heptanol

[1838-73-9]

C8H18O

MW = 130.23

112

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 5.5178 · 10−1 (combined temperature ranges, weighted), σc,uw = 2.7388 · 10−1 (combined temperature ranges, unweighted). T = 273.15 to 373.12 K ρ = A + BT + CT 2 + DT 3 + … 1.08833 · 103 −8.57031 · 10−1

Coefficient A B

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 273.20 283.15 293.15 303.15 313.15 333.15

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

853.53 ± 1.00 844.81 ± 1.00 836.96 ± 1.00 828.57 ± 1.00 820.34 ± 1.00 802.89 ± 1.00

−0.66 −0.85 −0.13 0.05 0.39 0.08

kg ⋅ m

Ref. (Symbol in Fig. 1)

) ) ) ) ) )

30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar(

T K 353.15 373.12 273.15 298.15 298.15

ρexp ± 2σ est −3

kg ⋅ m

785.61 ± 1.00 767.40 ± 1.00 853.70 ± 0.60 833.50 ± 0.60 835.00 ± 2.00

ρexp − ρcalc kg ⋅ m−3

−0.06 −1.16 −0.53 0.69 2.19

Ref. (Symbol in Fig. 1)

30-bin/dar( ) 30-bin/dar( ) 41-dor/gla( ) 41-dor/gla( ) 65-col/des(∆) cont.

Landolt-Börnstein New Series IV/8G

2.1.4 Alkanols, C8

125

ρ

ρ

Further references: [33-bri].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15

Landolt-Börnstein New Series IV/8G

ρ ± σ fit kg ⋅ m−3 856.93 ± 1.25 848.36 ± 1.22 839.79 ± 1.19 837.09 ± 1.17 832.81 ± 1.14

T K

300.00 310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 831.22 ± 1.13 822.65 ± 1.13 814.08 ± 1.09 805.51 ± 1.05 796.94 ± 1.01

T K

350.00 360.00 370.00 380.00

ρ ± σ fit kg ⋅ m−3 788.37 ± 1.01 779.80 ± 1.04 771.23 ± 1.13 762.66 ± 1.29

126

2.1.4 Alkanols, C8

4-Methyl-1-heptanol

[817-91-4]

C8H18O

MW = 130.23

113

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 5.6667 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.8889 · 10−1 (combined temperature ranges, unweighted). Coefficient A B

T = 273.15 to 373.35 K ρ = A + BT + CT 2 + DT 3 + … 1.03650 · 103 −7.73026 · 10−1

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

824.88 ± 1.00 817.13 ± 1.00 810.24 ± 1.00 802.57 ± 1.00 795.10 ± 1.00

−0.38 −0.49 0.35 0.41 0.67

Ref. (Symbol in Fig. 1)

) ) ) ) )

30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar(

T K

333.15 353.15 373.35 273.15 298.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

779.42 ± 1.00 763.77 ± 1.00 746.88 ± 1.00 824.60 ± 1.00 806.50 ± 1.00

0.45 0.26 −1.01 −0.75 0.48

Ref. (Symbol in Fig. 1)

) ) ) ) )

30-bin/dar( 30-bin/dar( 30-bin/dar( 41-dor/gla( 41-dor/gla(

ρ

ρ

273.27 283.15 293.15 303.15 313.15

ρexp ± 2σ est

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont. Landolt-Börnstein New Series IV/8G

2.1.4 Alkanols, C8

127

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ).

ρ ± σ fit kg ⋅ m−3

T K

827.78 ± 1.07 820.05 ± 1.04 812.32 ± 1.02 809.89 ± 1.01 806.02 ± 1.01

270.00 280.00 290.00 293.15 298.15

ρ ± σ fit kg ⋅ m−3

T K

804.59 ± 1.00 796.86 ± 1.00 789.13 ± 1.01 781.40 ± 1.02 773.67 ± 1.04

300.00 310.00 320.00 330.00 340.00

4-Methyl-2-heptanol

ρ ± σ fit kg ⋅ m−3

T K

[56298-90-9]

350.00 360.00 370.00 380.00

C8H18O

765.94 ± 1.08 758.21 ± 1.12 750.48 ± 1.16 742.75 ± 1.22

MW = 130.23

114

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 1.0278 · 10−1 (combined temperature ranges, weighted), σc,uw = 5.1187 · 10−2 (combined temperature ranges, unweighted). T = 273.15 to 373.13 K ρ = A + BT + CT 2 + DT 3 + … 9.32872 · 102 −1.40659 · 10−1 −1.03498 · 10−3

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 273.20 283.15 293.15 303.15 313.15 1)

ρexp ± 2σ est −3

kg ⋅ m

817.33 ± 1.00 809.78 ± 1.00 802.57 ± 1.00 795.04 ± 1.00 787.40 ± 1.00

ρexp − ρcalc Ref. (Symbol in Fig. 1) kg ⋅ m−3

0.13 −0.29 −0.13 −0.08 0.07

) ) ) ) )

30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar(

T K 333.15 353.15 373.13 273.15 298.15

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

771.31 ± 1.00 755.23 ± 1.00 736.27 ± 1.00 817.30 ± 0.60 799.00 ± 0.60

0.17 1.11 −0.02 0.07 0.07

kg ⋅ m

Ref. (Symbol in Fig. 1)

) ) ) )

30-bin/dar( 30-bin/dar1) 30-bin/dar( 41-dor/gla( 41-dor/gla(

Not included in Fig. 1.

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15

ρ ± σ fit kg ⋅ m−3 819.44 ± 0.99 812.35 ± 0.91 805.04 ± 0.90 802.70 ± 0.91 798.93 ± 0.92

T K

300.00 310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 797.53 ± 0.93 789.81 ± 0.97 781.88 ± 1.01 773.75 ± 1.03 765.40 ± 1.05

T K

350.00 360.00 370.00 380.00

ρ ± σ fit kg ⋅ m−3 756.86 ± 1.09 748.10 ± 1.17 739.14 ± 1.31 729.97 ± 1.52

cont. Landolt-Börnstein New Series IV/8G

128

2.1.4 Alkanols, C8

ρ

ρ

4-Methyl-2-heptanol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

4-Methyl-3-heptanol

[14979-39-6]

C8H18O

MW = 130.23

115

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 2.8281 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.0734 · 10−1 (combined temperature ranges, unweighted). T = 273.15 to 373.56 K ρ = A + BT + CT 2 + DT 3 + … 9.85558 · 102 −4.61789 · 10−1 −6.04236 · 10−4

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

273.18 283.15 293.15 303.15 313.15 333.15

ρexp ± 2σ est −3

kg ⋅ m

814.33 ± 1.00 805.67 ± 1.00 798.02 ± 1.00 789.76 ± 1.00 781.62 ± 1.00 764.47 ± 1.00

ρexp − ρcalc kg ⋅ m−3

0.02 −0.69 −0.24 −0.28 −0.08 −0.18

Ref. (Symbol in Fig. 1)

) ) ) ) ) )

30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar(

T K

353.15 373.56 273.15 293.15 298.15

ρexp ± 2σ est

ρexp − ρcalc

−3

kg ⋅ m−3

Ref. (Symbol in Fig. 1)

747.50 ± 1.00 728.86 ± 1.00 814.50 ± 0.60 798.60 ± 0.60 794.60 ± 0.60

0.38 0.13 0.16 0.34 0.44

30-bin/dar( 30-bin/dar( 41-dor/gla( 41-dor/gla( 41-dor/gla(

kg ⋅ m

) ) ) ) ) cont.

Landolt-Börnstein New Series IV/8G

2.1.4 Alkanols, C8

129

ρ

ρ

Further references: [12-bje].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15

Landolt-Börnstein New Series IV/8G

ρ ± σ fit kg ⋅ m−3 816.83 ± 0.95 808.89 ± 0.87 800.82 ± 0.87 798.26 ± 0.87 794.16 ± 0.89

T K

300.00 310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 792.64 ± 0.90 784.34 ± 0.94 775.91 ± 0.98 767.37 ± 1.00 758.70 ± 1.02

T K

350.00 360.00 370.00 380.00

ρ ± σ fit kg ⋅ m−3 749.91 ± 1.05 741.01 ± 1.12 731.98 ± 1.24 722.83 ± 1.44

130

2.1.4 Alkanols, C8

4-Methyl-4-heptanol

[598-01-6]

C8H18O

MW = 130.23

116

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 5.8580 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.7570 · 10−1 (combined temperature ranges, unweighted). T = 273.15 to 373.42 K ρ = A + BT + CT 2 + DT 3 + … 9.96959 · 102 −3.50068 · 10−1 −8.24303 · 10−4

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 289.85 273.26 283.15 293.15 303.15 313.15 333.15 353.15 373.42 273.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

826.90 ± 2.00 840.12 ± 1.00 831.67 ± 1.00 823.99 ± 1.00 815.79 ± 1.00 807.56 ± 1.00 789.45 ± 1.00 771.13 ± 1.00 751.48 ± 1.00 839.30 ± 1.00

0.66 0.37 −0.08 0.49 0.71 1.06 0.60 0.60 0.19 −0.54

Ref. (Symbol in Fig. 1) 19-eyk(◆) 30-bin/dar(∆) 30-bin/dar(∆) 30-bin/dar(∆) 30-bin/dar(∆) 30-bin/dar(∆) 30-bin/dar(∆) 30-bin/dar(∆) 30-bin/dar(∆) 39-owe/qua( )

T K 298.15 308.15 318.15 328.15 338.15 273.15 293.15 298.15 293.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

818.30 ± 1.00 809.60 ± 1.00 801.00 ± 1.00 792.50 ± 1.00 783.90 ± 1.00 839.70 ± 0.60 824.10 ± 0.60 820.20 ± 0.60 822.70 ± 1.00

−1.01 −1.21 −1.15 −0.82 −0.43 −0.14 0.60 0.89 −0.80

Ref. (Symbol in Fig. 1)

39-owe/qua( ) 39-owe/qua( ) 39-owe/qua( ) 39-owe/qua( ) 39-owe/qua( ) 41-dor/gla( ) 41-dor/gla( ) 41-dor/gla( ) 59-yur/bel(∇)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15

ρ ± σ fit kg ⋅ m−3 842.35 ± 1.07 834.31 ± 1.01 826.12 ± 0.99 823.50 ± 0.99 819.31 ± 1.00

T K

300.00 310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 817.75 ± 1.00 809.22 ± 1.01 800.53 ± 1.02 791.67 ± 1.03 782.65 ± 1.04

T K

350.00 360.00 370.00 380.00

ρ ± σ fit kg ⋅ m−3 773.46 ± 1.06 764.10 ± 1.13 754.59 ± 1.24 744.90 ± 1.43

cont.

Landolt-Börnstein New Series IV/8G

131

ρ

ρ

2.1.4 Alkanols, C8

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

5-Methyl-1-heptanol

[7212-53-5]

C8H18O

MW = 130.23

117

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 2.1134 · 10−1 (combined temperature ranges, weighted), σc,uw = 9.5153 · 10−2 (combined temperature ranges, unweighted). Coefficient A B C

T = 273.15 to 373.22 K ρ = A + BT + CT 2 + DT 3 + … 9.74236 · 102 −3.44128 · 10−1 −6.33911 · 10−4

cont.

Landolt-Börnstein New Series IV/8G

132

2.1.4 Alkanols, C8

5-Methyl-1-heptanol (cont.) Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

−3

kg ⋅ m

833.33 ± 1.00 825.76 ± 1.00 818.80 ± 1.00 811.56 ± 1.00 804.38 ± 1.00 789.20 ± 1.00

0.51 −0.21 −0.08 −0.10 0.07 −0.03

kg ⋅ m

Ref. (Symbol in Fig. 1)

) ) ) ) ) )

30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar(

T K

353.15 373.22 273.15 293.15 298.15

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

774.23 ± 1.00 757.06 ± 1.00 832.90 ± 0.60 818.70 ± 0.60 815.20 ± 0.60

0.58 −0.44 −0.04 −0.18 −0.08

kg ⋅ m

Ref. (Symbol in Fig. 1)

) ) ) ) )

30-bin/dar( 30-bin/dar( 41-dor/gla( 41-dor/gla( 41-dor/gla(

ρ

ρ

273.32 283.15 293.15 303.15 313.15 333.15

ρexp − ρcalc

−3

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15

ρ ± σ fit kg ⋅ m−3 835.11 ± 0.95 828.18 ± 0.87 821.13 ± 0.87 818.88 ± 0.87 815.28 ± 0.89

T K

300.00 310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 813.94 ± 0.90 806.64 ± 0.94 799.20 ± 0.98 791.64 ± 1.00 783.95 ± 1.02

T K

350.00 360.00 370.00 380.00

ρ ± σ fit kg ⋅ m−3 776.14 ± 1.05 768.19 ± 1.12 760.13 ± 1.24 751.93 ± 1.44

Landolt-Börnstein New Series IV/8G

2.1.4 Alkanols, C8 L(+)-5-Methyl-1-heptanol

[500006-90-6]

133 C8H18O

MW = 130.23

118

C8H18O

MW = 130.23

119

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

298.15

Ref.

−3

kg ⋅ m

825.9 ± 0.6

62-lar/sal

5-Methyl-2-heptanol

[54630-50-1]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 3.6541 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.7122 · 10−1 (combined temperature ranges, unweighted). T = 273.15 to 373.50 K ρ = A + BT + CT 2 + DT 3 + … 8.98516 · 102 2.01122 · 10−1 −1.67280 · 10−3

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 273.20 283.15 293.15 303.15 313.15 333.15 1)

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

828.78 ± 1.00 820.55 ± 1.00 813.34 ± 1.00 805.22 ± 1.00 797.45 ± 1.00 780.88 ± 1.00

0.17 -0.80 −0.38 −0.54 −0.01 1.02

Ref. (Symbol in Fig. 1)

) ) ) ) ) )

30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar(

T K 353.15 373.50 273.15 293.15 298.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

764.06 ± 1.00 740.14 ± 1.00 829.00 ± 0.60 813.80 ± 0.60 810.00 ± 0.60

3.14 −0.13 0.36 0.08 0.22

Ref. (Symbol in Fig. 1) 30-bin/dar1) 30-bin/dar( 41-dor/gla( 41-dor/gla( 41-dor/gla(

) ) ) )

Not included in Fig. 1.

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15

ρ ± σ fit kg ⋅ m−3 830.87 ± 0.95 823.68 ± 0.87 816.16 ± 0.86 813.72 ± 0.87 809.78 ± 0.89

T K

300.00 310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 808.30 ± 0.90 800.11 ± 0.94 791.58 ± 0.98 782.72 ± 1.01 773.52 ± 1.04

T K

350.00 360.00 370.00 380.00

ρ ± σ fit kg ⋅ m−3 763.99 ± 1.08 754.12 ± 1.16 743.92 ± 1.30 733.39 ± 1.50

cont.

Landolt-Börnstein New Series IV/8G

134

2.1.4 Alkanols, C8

ρ

ρ

5-Methyl-2-heptanol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

5-Methyl-3-heptanol

[18720-65-5]

C8H18O

MW = 130.23

120

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 9.4864 · 10−1 (combined temperature ranges, weighted), σc,uw = 2.9572 · 10−1 (combined temperature ranges, unweighted). Coefficient A B

T = 273.15 to 373.20 K ρ = A + BT + CT 2 + DT 3 + … 1.07627 · 103 −8.79191 · 10−1

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 273.19 283.15 293.15 303.15 313.15 333.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

834.52 ± 1.00 826.04 ± 1.00 817.86 ± 1.00 809.59 ± 1.00 801.28 ± 1.00 783.82 ± 1.00

−1.57 −1.29 −0.68 −0.15 0.33 0.45

Ref. (Symbol in Fig. 1)

) ) ) ) ) )

30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar(

T K 353.15 373.20 296.15 273.15 298.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

766.11 ± 1.00 748.00 ± 1.00 816.00 ± 2.00 836.70 ± 0.60 816.20 ± 0.60

0.32 −0.16 0.10 0.58 2.06

Ref. (Symbol in Fig. 1)

30-bin/dar( ) 30-bin/dar( ) 31-lev/mar-4(∆) 41-dor/gla( ) 41-dor/gla( ) cont. Landolt-Börnstein New Series IV/8G

2.1.4 Alkanols, C8

135

ρ

ρ

Further references: [12-gue, 31-pow/sec, 59-mac/bar].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15

Landolt-Börnstein New Series IV/8G

ρ ± σ fit kg ⋅ m−3 838.89 ± 1.25 830.10 ± 1.22 821.31 ± 1.19 818.54 ± 1.17 814.14 ± 1.14

T K

300.00 310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 812.51 ± 1.13 803.72 ± 1.12 794.93 ± 1.08 786.14 ± 1.03 777.35 ± 1.00

T K

350.00 360.00 370.00 380.00

ρ ± σ fit kg ⋅ m−3 768.55 ± 0.99 759.76 ± 1.03 750.97 ± 1.14 742.18 ± 1.31

136

2.1.4 Alkanols, C8

6-Methyl-1-heptanol

[1653-40-3]

C8H18O

MW = 130.23

121

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 1.1940 · 10−1 (combined temperature ranges, weighted), σc,uw = 5.7073 · 10−2 (combined temperature ranges, unweighted). Coefficient A B C

T = 273.15 to 373.57 K ρ = A + BT + CT 2 + DT 3 + … 9.65307 · 102 −2.92230 · 10−1 −6.81907 · 10−4

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

273.37 283.15 293.15 303.15 313.15 333.15

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

839.14 ± 3.00 827.61 ± 1.00 820.95 ± 1.00 814.07 ± 1.00 806.97 ± 1.00 792.14 ± 1.00

4.68 −0.28 −0.09 0.02 0.04 −0.13

Ref. (Symbol in Fig. 1) 30-bin/dar1) 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar(

) ) ) ) )

T K

353.15 373.57 273.15 293.15 298.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

777.42 ± 1.00 760.86 ± 1.00 834.70 ± 0.60 821.10 ± 0.60 817.60 ± 0.60

0.36 −0.12 0.09 0.06 0.04

Ref. (Symbol in Fig. 1)

) ) ) ) )

30-bin/dar( 30-bin/dar( 41-dor/gla( 41-dor/gla( 41-dor/gla(

Not included in Fig. 1.

ρ

ρ

1)

ρexp ± 2σ est

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont.

Landolt-Börnstein New Series IV/8G

2.1.4 Alkanols, C8

137

Further references: [16-lev/all]. Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ).

ρ ± σ fit kg ⋅ m−3

T K

836.69 ± 0.89 830.02 ± 0.81 823.21 ± 0.83 821.04 ± 0.85 817.56 ± 0.88

270.00 280.00 290.00 293.15 298.15

ρ ± σ fit kg ⋅ m−3

T K

816.27 ± 0.90 809.18 ± 0.96 801.97 ± 1.01 794.61 ± 1.04 787.12 ± 1.06

300.00 310.00 320.00 330.00 340.00

6-Methyl-2-heptanol

[4730-22-7]

ρ ± σ fit kg ⋅ m−3

T K

350.00 360.00 370.00 380.00

C8H18O

779.49 ± 1.07 771.73 ± 1.11 763.83 ± 1.21 755.79 ± 1.39

MW = 130.23

122

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 1.6961 · 10−1 (combined temperature ranges, weighted), σc,uw = 8.6825 · 10−2 (combined temperature ranges, unweighted). T = 273.15 to 373.37 K ρ = A + BT + CT 2 + DT 3 + … 9.63426 · 102 −3.06269 · 10−1 −7.74629 · 10−4

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 284.15 273.17 283.15 293.15 303.15 313.15

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

814.10 ± 2.00 822.37 ± 1.00 814.46 ± 1.00 807.04 ± 1.00 799.17 ± 1.00 791.39 ± 1.00

0.24 0.41 −0.14 −0.03 −0.22 −0.17

kg ⋅ m

Ref. (Symbol in Fig. 1) 28-esc(∆) 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar(

) ) ) ) )

T K 333.15 353.15 373.37 273.15 293.15 298.15

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

775.43 ± 1.00 759.07 ± 1.00 740.47 ± 1.00 821.90 ± 0.60 807.10 ± 0.60 803.40 ± 0.60

0.01 0.41 −0.62 −0.07 0.03 0.15

kg ⋅ m

Ref. (Symbol in Fig. 1)

) ) ) ) ) )

30-bin/dar( 30-bin/dar( 30-bin/dar( 41-dor/gla( 41-dor/gla( 41-dor/gla(

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15

ρ ± σ fit kg ⋅ m−3 824.26 ± 1.03 816.94 ± 1.05 809.46 ± 1.06 807.07 ± 1.05 803.25 ± 1.04

T K

300.00 310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 801.83 ± 1.03 794.04 ± 0.98 786.10 ± 0.93 778.00 ± 0.90 769.75 ± 0.95

T K

350.00 360.00 370.00 380.00

ρ ± σ fit kg ⋅ m−3 761.34 ± 1.12 752.78 ± 1.27 744.06 ± 1.33 735.19 ± 1.47

cont.

Landolt-Börnstein New Series IV/8G

138

2.1.4 Alkanols, C8

6-Methyl-2-heptanol (cont.)

ρ

ρ

Further references: [08-bue, 08-bue-1, 12-gue-2, 14-wal-1, 52-her/zao, 53-her/zao, 62-mir/fed].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

6-Methyl-3-heptanol

[18720-66-6]

C8H18O

MW = 130.23

123

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 7.5441 · 10−1 (combined temperature ranges, weighted), σc,uw = 3.0306 · 10−1 (combined temperature ranges, unweighted). Coefficient A B

T = 273.15 to 373.32 K ρ = A + BT + CT 2 + DT 3 + … 1.02123 · 103 −8.20546 · 10−1

cont. Landolt-Börnstein New Series IV/8G

2.1.4 Alkanols, C8

139

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

−3

kg ⋅ m

796.69 ± 1.00 788.58 ± 1.00 781.43 ± 1.00 773.46 ± 1.00 765.81 ± 1.00 748.56 ± 1.00

−0.19 −0.32 0.74 0.97 1.53 0.69

kg ⋅ m

273.42 283.15 293.15 303.15 313.15 333.15

ρexp − ρcalc

−3

Ref. (Symbol in Fig. 1)

) ) ) ) ) )

30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar(

T K

353.15 373.32 273.15 293.15 298.15

ρexp ± 2σ est −3

kg ⋅ m

731.42 ± 1.00 712.81 ± 1.00 796.00 ± 0.60 780.50 ± 0.60 776.60 ± 0.60

ρexp − ρcalc kg ⋅ m−3

−0.04 −2.10 −1.10 −0.19 0.01

Ref. (Symbol in Fig. 1)

) ) ) ) )

30-bin/dar( 30-bin/dar( 41-dor/gla( 41-dor/gla( 41-dor/gla(

ρ

ρ

Further references: [08-bue-1, 33-bri, 44-hen/mat].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont.

Landolt-Börnstein New Series IV/8G

140

2.1.4 Alkanols, C8

6-Methyl-3-heptanol (cont.) Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K 270.00 280.00 290.00 293.15 298.15

ρ ± σ fit kg ⋅ m−3

ρ ± σ fit kg ⋅ m−3

T K

799.69 ± 0.87 791.48 ± 0.86 783.28 ± 0.86 780.69 ± 0.87 776.59 ± 0.87

775.07 ± 0.88 766.87 ± 0.90 758.66 ± 0.92 750.45 ± 0.96 742.25 ± 1.00

300.00 310.00 320.00 330.00 340.00

3-Methyl-2-(1-methylethyl)-1-butanol

T K

[18593-92-5]

350.00 360.00 370.00 380.00

ρ ± σ fit kg ⋅ m−3 734.04 ± 1.05 725.84 ± 1.10 717.63 ± 1.16 709.43 ± 1.22

C8H18O

MW = 130.23

124

C8H18O

MW = 130.23

125

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 56-sar/new 842.5 ± 1.0 1-Octanol

[111-87-5]

Tc = 652.60 K [89-tej/lee]

ρc = 266.00 kg·m−3 [89-tej/lee]

Table 1. Coefficients for the polynomial expansion equations. Standard deviations (see introduction): σ = 3.5218 · 10−1 (low temperature range), σc,w = (2.6366 · 10−1 combined temperature ranges, weighted), σc,uw = 3.0252 · 10−1 (combined temperature ranges, unweighted).

Coefficient

T = 258.08 to 530.00 K ρ = A + BT + CT 2 + DT 3 + …

1.02020 · 103 −7.81865 · 10-1 8.70573 · 10−4 −1.61006 · 10−6

A B C D

T = 530.00 to 652.60 K ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)] [ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] 1.11884 −1.68799 · 10−2 8.96699 · 10−5 −1.31742 · 10−7

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 303.15 818.60 ± 0.60 0.27 crystal 78.15 1023.0 ± 3.0 30-bil/fis-1 303.15 818.60 ± 0.40 0.27 194.15 1001.0 ± 3.0 30-bil/fis-1 313.15 811.50 ± 0.40 0.21 323.15 804.20 ± 0.50 0.08 liquid 263.15 846.10 ± 0.50 0.70 29-smy/sto(✕ ) 333.15 797.00 ± 0.50 0.19 273.15 839.10 ± 0.50 0.33 29-smy/sto1) 273.15 838.46 ± 0.20 −0.31 283.15 832.20 ± 0.50 0.14 29-smy/sto1) 298.15 821.35 ± 0.20 −0.45 293.15 825.30 ± 0.40 0.05 29-smy/sto1) 273.15 837.50 ± 0.50 −1.27 293.15 825.30 ± 0.60 0.05 29-smy/sto1) 293.15 822.70 ± 0.52 −2.55 1)

Not included in Fig. 1.

Ref. (Symbol in Fig. 1) 29-smy/sto1) 29-smy/sto1) 29-smy/sto1) 29-smy/sto1) 29-smy/sto1) 32-ell/rei(✕ ) 32-ell/rei1) 58-cos/bow1) 58-cos/bow1)

cont. Landolt-Börnstein New Series IV/8G

2.1.4 Alkanols, C8

141

Table 2. (cont.) T K

313.15 333.15 353.15 373.15 393.15 413.15 433.15 453.15 473.15 493.15 513.15 533.15 553.15 273.15 273.15 293.15 313.15 333.15 353.15 373.15 393.15 413.15 433.15 453.15 473.15 493.15 513.15 533.15 553.15 573.15 593.15 613.15 633.15 643.15 258.08 258.33 286.14 293.15 303.15 313.15 1)

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

809.10 ± 0.54 794.80 ± 0.56 780.40 ± 0.58 764.30 ± 0.60 747.70 ± 0.62 730.50 ± 0.64 713.10 ± 0.66 695.10 ± 0.68 675.60 ± 0.70 655.30 ± 0.72 635.10 ± 1.50 613.70 ± 1.50 590.00 ± 2.00 838.93 ± 0.10 843.00 ± 1.50 827.00 ± 1.50 812.00 ± 1.50 797.00 ± 1.50 782.00 ± 1.50 767.00 ± 1.50 750.00 ± 1.50 733.00 ± 1.50 714.00 ± 1.50 696.00 ± 1.50 677.00 ± 1.50 657.00 ± 1.50 637.00 ± 1.50 615.00 ± 1.50 592.00 ± 1.50 565.00 ± 1.50 534.00 ± 1.50 500.00 ± 2.00 444.00 ± 2.00 400.00 ± 3.00 849.12 ± 0.17 848.86 ± 0.17 829.91 ± 0.17 825.10 ± 0.17 818.18 ± 0.16 811.19 ± 0.16

−2.19 −2.01 −1.34 −1.71 −1.83 −1.73 −0.92 0.26 0.99 2.06 4.43 6.81 4.73 0.16 4.23 1.75 0.71 0.19 0.26 0.99 0.47 0.77 −0.02 1.16 2.39 3.76 6.33 8.11 6.73 0.79 −4.26 −0.69 2.66 4.51 0.40 0.30 −0.12 −0.15 −0.15 −0.10

kg ⋅ m

Ref. (Symbol in Fig. 1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow1) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 59-mck/ski(∆) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 73-fin(✕ ) 73-fin(✕ ) 73-fin(✕ ) 73-fin1) 73-fin1) 73-fin(✕ )

T K

323.07 333.12 333.18 293.15 298.15 303.15 320.00 340.00 360.00 380.00 400.00 420.00 440.00 460.00 470.00 480.00 490.00 293.15 298.15 303.15 298.15 308.15 318.15 333.15 298.15 298.15 283.15 298.15 313.15 323.15 328.15 333.15 338.15 343.15 348.15 353.15 358.15 363.15 373.15

ρexp ± 2σ est −3

kg ⋅ m

804.15 ± 0.16 796.87 ± 0.16 796.85 ± 0.16 824.99 ± 0.25 821.57 ± 0.25 818.11 ± 0.25 806.27 ± 0.25 791.73 ± 0.25 776.47 ± 0.25 760.46 ± 0.25 743.64 ± 0.30 725.96 ± 0.30 707.32 ± 0.30 687.82 ± 0.30 677.71 ± 0.30 667.39 ± 0.35 656.77 ± 0.35 825.23 ± 0.10 821.87 ± 0.10 818.30 ± 0.10 822.60 ± 0.20 815.52 ± 0.20 808.42 ± 0.20 797.58 ± 0.20 821.79 ± 0.02 820.85 ± 0.10 831.83 ± 0.20 821.59 ± 0.20 811.14 ± 0.20 804.18 ± 0.10 801.15 ± 0.10 796.80 ± 0.10 793.35 ± 0.10 789.36 ± 0.10 785.43 ± 0.10 781.89 ± 0.10 777.90 ± 0.10 773.73 ± 0.10 765.97 ± 0.10

ρexp − ρcalc kg ⋅ m−3

−0.03 0.04 0.06 −0.26 −0.23 −0.22 −0.12 0.01 0.04 0.01 −0.06 −0.14 −0.25 −0.22 −0.16 −0.03 0.08 −0.02 0.07 −0.03 0.80 0.70 0.70 0.77 −0.01 −0.95 −0.23 −0.21 −0.15 0.06 0.67 −0.01 0.25 0.00 −0.14 0.15 0.02 −0.24 −0.04

Ref. (Symbol in Fig. 1) 73-fin(✕ ) 73-fin(✕ ) 73-fin(✕ ) 76-hal/ell1) 76-hal/ell1) 76-hal/ell1) 76-hal/ell1) 76-hal/ell1) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 76-hal/ell(✕ ) 78-jel/leo(◆) 78-jel/leo(◆) 78-jel/leo(◆) 79-dia/tar1) 79-dia/tar(✕ ) 79-dia/tar(✕ ) 79-dia/tar1) 79-kiy/ben( ) 84-sak/nak(∇) 86-hei/sch(✕ ) 86-hei/sch1) 86-hei/sch(✕ ) 93-gar/ban-1( 93-gar/ban-1( 93-gar/ban-1( 93-gar/ban-1( 93-gar/ban-1( 93-gar/ban-1( 93-gar/ban-1( 93-gar/ban-1( 93-gar/ban-1( 93-gar/ban-1(

) ) ) ) ) ) ) ) ) )

Not included in Fig. 1.

Further references: [1869-zin, 1884-per, 1884-zan, 1886-gar, 1890-gar, 13-har, 14-low, 19-beh, 19-eyk, 27-ver/coo, 29-mah/das, 31-def, 32-kom/tal, 33-ano, 33-but/tho, 33-nev/jat, 35-but/ram, 35-saw, 37-oli, 41-dor/gla, 41-hus/age, 45-add, 48-jon/bow, 48-vog-2, 48-wei, 49-dre/mar, 49-tsv/mar, 50-mum/phi, 50-sac/sau, 52-coo, 52-eri-1, 53-par/cha, 56-goe/mcc, 56-goe/mcc-1, 62-bro/smi, 62-gei/fru, 62-par/mis, 64-blo/hag, 67-gol/per, 69-kat/pat, 73-min/rue, 75-mat/fer, 78-ast, 78-tre/ben, 80-sue/mul,] cont. Landolt-Börnstein New Series IV/8G

142

2.1.4 Alkanols, C8

1-Octanol (cont.) Further references (cont.)

ρ

ρ

[81-sjo/dyh, 82-aww/pet, 82-kat/wat, 82-ort, 82-ven/dha, 83-rau/ste, 85-fer/pin, 85-ort/paz-1, 85-sar/paz, 85-zhu, 86-ash/sri, 86-dew/meh, 86-wag/hei, 87-dew/meh, 88-ort/gar, 89-ala/sal, 89-dew/gup, 89-mat/mak-1, 89-vij/nai, 90-vij/nai, 91-ram/muk, 92-lie/sen-1, 93-yan/mae, 94-yu /tsa-1, 95-arc/bla, 95-cas/cal, 95-fra/jim, 95-fra/men, 95-sen/say, 96-elb].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

250.00 260.00 270.00 280.00 290.00 293.15

ρ ± σ fit kg ⋅ m−3 853.99 ± 0.25 847.47 ± 0.22 840.87 ± 0.19 834.18 ± 0.17 827.40 ± 0.16 825.25 ± 0.16

T K

298.15 300.00 310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 821.80 ± 0.15 820.52 ± 0.15 813.52 ± 0.15 806.39 ± 0.15 799.13 ± 0.15 791.72 ± 0.16

T K

350.00 360.00 370.00 380.00 390.00 400.00

ρ ± σ fit kg ⋅ m−3 784.16 ± 0.17 776.43 ± 0.18 768.54 ± 0.20 760.45 ± 0.22 752.18 ± 0.25 743.70 ± 0.28 cont.

Landolt-Börnstein New Series IV/8G

2.1.4 Alkanols, C8

143

Table 3. (cont.)

ρ ± σ fit kg ⋅ m−3

T K

T K

735.01 ± 0.31 726.10 ± 0.34 716.95 ± 0.38 707.57 ± 0.42 697.93 ± 0.47 688.04 ± 0.52 677.87 ± 0.57 667.42 ± 0.63 656.69 ± 0.70

410.00 420.00 430.00 440.00 450.00 460.00 470.00 480.00 490.00

500.00 510.00 520.00 530.00 540.00 550.00 560.00 570.00 580.00

2-Octanol

ρ ± σ fit kg ⋅ m−3 645.65 ± 0.77 634.31 ± 0.86 622.64 ± 0.95 610.65 ± 1.05 599.13 ± 1.80 588.51 ± 1.86 578.25 ± 1.93 567.70 ± 2.01 556.18 ± 2.10

[123-96-6]

ρ ± σ fit kg ⋅ m−3

T K

590.00 600.00 610.00 620.00 630.00 640.00 650.00

C8H18O

542.93 ± 2.21 527.10 ± 2.33 507.71 ± 2.47 483.56 ± 2.64 452.84 ± 3.85 411.94 ± 4.10 344.17 ± 5.40

MW = 130.23

126

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 1.9507 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.1763 · 10−1 (combined temperature ranges, unweighted). T = 273.15 to 452.15 K ρ = A + BT + CT 2 + DT 3 + … 9.55354 · 102 −1.73168 · 10−1 −9.75788 · 10−4

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 452.15 452.15 273.15 298.15 293.15 293.15

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

678.10 ± 1.00 678.20 ± 1.00 835.30 ± 0.60 817.00 ± 0.60 820.50 ± 0.50 820.80 ± 0.50

0.53 0.63 0.05 0.02 −0.23 0.07

kg ⋅ m

Ref. (Symbol in Fig. 1) 1883-sch-3(✕ ) 1883-sch-3(✕ ) 41-dor/gla(∆) 41-dor/gla(∆) 46-bra(✕ ) 52-coo(◆)

T K 293.15 293.15 298.15 303.15 308.15

ρexp ± 2σ est −3

kg ⋅ m

820.60 ± 0.50 820.00 ± 0.40 817.10 ± 0.40 813.00 ± 0.40 809.20 ± 0.40

ρexp − ρcalc kg ⋅ m−3

−0.13 −0.73 0.12 −0.18 −0.13

Ref. (Symbol in Fig. 1) 62-gei/fru(∇) 90-bar/paz( ) 93-ami/rai( ) 93-ami/rai( ) 93-ami/rai( )

Further references: [1863-gla/dal, 1880-bru-1, 1884-per, 11-pic/ken, 19-beh, 19-eyk, 33-whi/her, 36-par, 37-zep, 42-mul, 45-add, 50-naz/fis, 53-ani-1, 57-tra/bat, 70-puz/bul].

cont. Landolt-Börnstein New Series IV/8G

144

2.1.4 Alkanols, C8

ρ

ρ

2-Octanol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15 300.00 310.00 320.00

ρ ± σ fit kg ⋅ m−3 837.46 ± 0.38 830.37 ± 0.37 823.07 ± 0.39 820.73 ± 0.40 816.98 ± 0.42 815.58 ± 0.43 807.90 ± 0.48 800.02 ± 0.53

T K

330.00 340.00 350.00 360.00 370.00 380.00 390.00 400.00

ρ ± σ fit kg ⋅ m−3 791.95 ± 0.58 783.68 ± 0.63 775.21 ± 0.67 766.55 ± 0.71 757.70 ± 0.75 748.65 ± 0.79 739.40 ± 0.82 729.96 ± 0.85

T K

410.00 420.00 430.00 440.00 450.00 460.00

ρ ± σ fit kg ⋅ m−3 720.33 ± 0.88 710.49 ± 0.92 700.47 ± 0.95 690.25 ± 0.99 679.83 ± 1.04 669.22 ± 1.10

Landolt-Börnstein New Series IV/8G

2.1.4 Alkanols, C8 (R)-(-)-2-Octanol

[5978-70-1]

145 C8H18O

MW = 130.23

127

C8H18O

MW = 130.23

128

C8H18O

MW = 130.23

129

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est

T K

298.15 298.15 298.15

Ref.

−3

kg ⋅ m

815.2 ± 1.0 816.0 ± 2.0 815.4 ± 1.0

55-ber/sch 56-goe/mcc Recommended

(RS)-2-Octanol

[4128-31-8]

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 0.189. Coefficient ρ = A + BT 1043.06 A B −0.760 Table 2. Experimental values with uncertainties and deviation from calculated values. T K 293.15 293.15 298.15

ρexp ± 2σ est

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−3

kg ⋅ m

820.2 ± 1.0 820.2 ± 1.0 817.0 ± 2.0

−0.07 −0.07 0.53

39-cop/gos 47-kor/lic 56-goe/mcc

Table 3. Recommended values. T K 290.00 293.15 298.15

ρexp ± 2σ est kg ⋅ m−3

822.7 ± 1.3 820.3 ± 1.2 816.5 ± 1.3

(S)-(+)-2-Octanol

[6169-06-8]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 4.6275 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.8230 · 10−1 (combined temperature ranges, unweighted). Coefficient A B

T = 273.15 to 355.65 K ρ = A + BT + CT 2 + DT 3 + … 1.03721 · 103 −7.40112 · 10−1

cont. Landolt-Börnstein New Series IV/8G

146

2.1.4 Alkanols, C8

(S)-(+)-2-Octanol (cont.) Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

1)

kg ⋅ m

Ref. (Symbol in Fig. 1)

822.90 ± 2.00 822.10 ± 2.00 835.03 ± 2.00 823.01 ± 2.00 834.10 ± 1.00 821.60 ± 1.00 810.70 ± 1.00

0.43 1.85 −0.02 6.47 −0.95 −0.27 −0.29

07-pic/ken(✕ ) 07-pic/ken(✕ ) 32-ell/rei(◆) 32-ell/rei1) 37-pat/hol( ) 37-pat/hol( ) 37-pat/hol( )

kg ⋅ m

290.15 293.15 273.15 298.15 273.15 290.95 305.65

ρexp − ρcalc

−3

−3

T K

320.45 333.45 346.75 355.65 293.15 293.15 298.15

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

799.70 ± 1.00 790.20 ± 1.00 780.30 ± 1.00 773.90 ± 1.00 820.10 ± 1.00 820.10 ± 1.00 817.00 ± 1.00

−0.34 −0.22 −0.28 −0.09 −0.15 −0.15 0.46

kg ⋅ m

Ref. (Symbol in Fig. 1)

37-pat/hol( ) 37-pat/hol( ) 37-pat/hol( ) 37-pat/hol( ) 39-cop/gos(∆) 47-kor/lic(∇) 56-goe/mcc( )

Not included in Fig. 1.

ρ

ρ

Further references: [12-pic/ken].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont.

Landolt-Börnstein New Series IV/8G

2.1.4 Alkanols, C8

147

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ).

ρ ± σ fit kg ⋅ m−3

T K

T K

837.38 ± 1.69 829.98 ± 1.50 822.58 ± 1.33 820.25 ± 1.29 816.54 ± 1.23

270.00 280.00 290.00 293.15 298.15

300.00 310.00 320.00 330.00 340.00

3-Octanol

ρ ± σ fit kg ⋅ m−3 815.18 ± 1.21 807.77 ± 1.11 800.37 ± 1.05 792.97 ± 1.04 785.57 ± 1.06

[589-98-0]

ρ ± σ fit kg ⋅ m−3

T K

350.00 360.00 370.00

C8H18O

778.17 ± 1.11 770.77 ± 1.20 763.37 ± 1.31

MW = 130.23

130

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 5.3499 · 10−1 (combined temperature ranges, weighted), σc,uw = 4.6865 · 10−1 (combined temperature ranges, unweighted). T = 273.15 to 373.01 K ρ = A + BT + CT 2 + DT 3 + … 9.61167 · 102 −1.85752 · 10−1 −9.98691 · 10−4

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

293.15 353.15 273.32 283.15 293.15 303.15 313.15

ρexp ± 2σ est

ρexp − ρcalc

−3

kg ⋅ m

Ref. (Symbol in Fig. 1)

824.70 ± 3.00 771.10 ± 3.00 835.49 ± 1.00 827.47 ± 1.00 820.88 ± 1.00 812.61 ± 1.00 804.44 ± 1.00

3.81 0.08 −0.30 −1.03 −0.01 −0.47 −0.62

13-pic/ken(∇) 13-pic/ken(∇) 30-bin/dar( ) 30-bin/dar( ) 30-bin/dar( ) 30-bin/dar( ) 30-bin/dar( )

kg ⋅ m

−3

T K

333.15 353.15 373.01 273.15 298.15 293.15

ρexp ± 2σ est

ρexp − ρcalc

−3

kg ⋅ m

Ref. (Symbol in Fig. 1)

787.53 ± 1.00 770.12 ± 1.00 751.09 ± 1.00 836.10 ± 0.60 816.00 ± 0.60 823.90 ± 2.00

−0.91 −0.90 −1.84 0.18 −1.01 3.01

30-bin/dar( ) 30-bin/dar( ) 30-bin/dar( ) 41-dor/gla( ) 41-dor/gla( ) 69-nav/tul(∆)

−3

kg ⋅ m

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15

ρ ± σ fit kg ⋅ m−3 838.21 ± 1.95 830.86 ± 1.90 823.31 ± 1.82 820.89 ± 1.74 817.01 ± 1.73

T K

300.00 310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 815.56 ± 1.72 807.61 ± 1.38 799.46 ± 1.49 791.11 ± 1.55 782.56 ± 1.55

T K

350.00 360.00 370.00 380.00

ρ ± σ fit kg ⋅ m−3 773.81 ± 1.55 764.87 ± 1.57 755.72 ± 1.59 746.37 ± 1.67

cont.

Landolt-Börnstein New Series IV/8G

148

2.1.4 Alkanols, C8

3-Octanol (cont.)

ρ

ρ

Further references: [56-woo/vio, 62-gei/fru].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

(RS)-3-Octanol

[20296-29-1]

C8H18O

MW = 130.23

131

C8H18O

MW = 130.23

132

Table 1. Experimental value with uncertainty. T K 295.35

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

817.7 ± 0.8

33-bri

(S)-(+)-3-Octanol

[22658-92-0]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

834.4 ± 1.0

57-shu/bel

Landolt-Börnstein New Series IV/8G

2.1.4 Alkanols, C8 4-Octanol

[589-62-8]

149 C8H18O

MW = 130.23

133

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 2.5809 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.7589 · 10−1 (combined temperature ranges, unweighted). Coefficient A B C

T = 273.15 to 373.32 K ρ = A + BT + CT 2 + DT 3 + … 9.65289 · 102 −2.26785 · 10−1 −9.21832 · 10−4

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

Ref. (Symbol in Fig. 1)

0.40 0.10 0.35 0.07 0.18 0.17

30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar( 30-bin/dar(

834.86 ± 1.00 827.27 ± 1.00 819.94 ± 1.00 811.89 ± 1.00 804.05 ± 1.00 787.59 ± 1.00

) ) ) ) ) )

T K

353.15 373.32 295.15 293.15 273.15 298.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

770.59 ± 1.00 752.16 ± 1.00 818.00 ± 2.00 817.80 ± 2.00 834.60 ± 0.60 815.90 ± 0.60

0.36 0.01 −0.05 −1.79 0.04 0.17

Ref. (Symbol in Fig. 1)

30-bin/dar( ) 30-bin/dar( ) 31-lev/mar-2(∆) 36-tuo(∇) 41-dor/gla( ) 41-dor/gla( )

ρ

ρ

273.29 283.15 293.15 303.15 313.15 333.15

ρexp ± 2σ est

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont.

Landolt-Börnstein New Series IV/8G

150

2.1.4 Alkanols, C8

4-Octanol (cont.) Further references: [06-bou/loc, 50-naz/fis, 62-gei/fru]. Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15

ρ ± σ fit kg ⋅ m−3

ρ ± σ fit kg ⋅ m−3

T K

836.86 ± 1.28 829.52 ± 1.27 822.00 ± 1.25 819.59 ± 1.26 815.73 ± 1.28

814.29 ± 1.29 806.40 ± 1.26 798.32 ± 1.17 790.06 ± 1.06 781.62 ± 0.97

300.00 310.00 320.00 330.00 340.00

2-Propyl-1-pentanol

[58175-57-8]

ρ ± σ fit kg ⋅ m−3

T K

350.00 360.00 370.00 380.00

772.99 ± 0.93 764.18 ± 1.00 755.18 ± 1.24 746.00 ± 1.64

C8H18O

MW = 130.23

134

C8H18O

MW = 130.23

135

Table 1. Experimental value with uncertainty. T K 294.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

900.0 ± 10.0

58-wie/thu

2,2,3-Trimethyl-3-pentanol

[7294-05-5]

Table 1. Fit with estimated B coefficient for 5 accepted points. Deviation σw = 0.823. Coefficient ρ = A + BT 1075.47 A B −0.780 Table 2. Experimental values with uncertainties and deviation from calculated values. T K

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

kg ⋅ m

293.15 849.0 ± 2.00 298.15 842.3 ± 1.00 298.15 843.4 ± 1.00 1)

ρexp − ρcalc

−3

2.19 −0.61 0.49

33-whi/lau 36-nor/has 36-nor/has

T K

ρexp ± 2σ est −3

kg ⋅ m

ρexp − ρcalc

Ref.

kg ⋅ m−3

298.15 842.0 ± 1.00 −0.91 293.15 831.0 ± 10.00 −15.81 293.15 847.3 ± 1.00 0.49

39-gin/col 57-pet/sus1) 62-gei/fru

Not included in calculation of linear coefficients.

Table 3. Recommended values. T K 290.00 293.15 298.15

ρexp ± 2σ est kg ⋅ m−3

849.3 ± 1.4 846.8 ± 1.3 842.9 ± 1.2

Landolt-Börnstein New Series IV/8G

2.1.4 Alkanols, C8 2,2,4-Trimethyl-1-pentanol

[123-44-4]

151 C8H18O

MW = 130.23

136

C8H18O

MW = 130.23

137

C8H18O

MW = 130.23

138

C8H18O

MW = 130.23

139

C8H18O

MW = 130.23

140

Table 1. Experimental and recommended values with uncertainties. T K 293.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

823.2 ± 10.0 838.4 ± 1.0 838.4 ± 1.0

25-ter1) 58-ano-3 Recommended

Not included in calculation of recommended value.

2,2,4-Trimethyl-3-pentanol

[5162-48-1]

Table 1. Experimental values with uncertainties. ρexp ± 2σ est

T K

293.15 293.15 293.15

Ref.

−3

kg ⋅ m

832.2 ± 1.0 832.6 ± 1.0 832.4 ± 1.0

51-smi/cre 62-gei/fru Recommended

2,3,3-Trimethyl-2-pentanol

[23171-85-9]

Table 1. Experimental values with uncertainties. ρexp ± 2σ est

T K

293.15 298.15 293.15

Ref.

kg ⋅ m−3

861.0 ± 2.0 815.1 ± 5.0 851.7 ± 2.0

33-whi/lau 36-nor/has 41-hus/gui

2,3,4-Trimethyl-1-pentanol

[6570-88-3]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

849.8 ± 1.0

58-per/can

2,3,4-Trimethyl-2-pentanol

[66576-26-9]

Table 1. Experimental values with uncertainties. ρexp ± 2σ est

T K

293.15 293.15 293.15

Ref.

kg ⋅ m−3

808.1 ± 2.0 808.0 ± 2.0 843.2 ± 2.0

Landolt-Börnstein New Series IV/8G

39-hus/gui 41-hus/gui 48-hus/kra

152

2.1.4 Alkanols, C8

2,3,4-Trimethyl-3-pentanol

[3054-92-0]

C8H18O

MW = 130.23

141

C8H18O

MW = 130.23

142

C8H18O

MW = 130.23

143

C8H18O

MW = 130.23

144

C8H18O

MW = 130.23

145

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

849.2 ± 2.0

26-sta

2,4,4-Trimethyl-1-pentanol

[16325-63-6]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

833.0 ± 2.0

40-sut

2,4,4-Trimethyl-2-pentanol

[690-37-9]

Table 1. Experimental and recommended values with uncertainties. T K 296.65 293.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

830.9 ± 6.0 822.5 ± 2.0 825.0 ± 2.0 823.7 ± 2.2

48-rit1) 41-hus/gui 41-whi/wil Recommended

Not included in calculation of recommended value.

3,3,4-Trimethyl-2-pentanol

[19411-41-7]

Table 1. Experimental and recommended values with uncertainties. T K

293.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

812.8 ± 4.0 855.7 ± 1.0 855.7 ± 1.0

08-bue1) 55-mes/pet Recommended

Not included in calculation of recommended value.

3,4,4-Trimethyl-2-pentanol

[10575-56-1]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

840.8 ± 1.0

41-whe

Landolt-Börnstein New Series IV/8G

2.1.5 Alkanols, C9

153

2.1.5 Alkanols, C9 2,2-Dimethyl-3-ethyl-3-pentanol

[66793-96-2]

C9H20O

MW = 144.26

146

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.250. Coefficient ρ = A + BT A 1097.33 B −0.820 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

293.15 293.15 298.15 1)

kg ⋅ m

−3

852.4 ± 3.0 857.2 ± 1.0 852.6 ± 1.0

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−4.55 0.25 −0.25

38-whi/mey1) 47-how/mea 47-how/mea

Not included in calculation of linear coefficients.

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 290.00 859.5 ± 0.9 293.15 857.0 ± 0.7 298.15 852.9 ± 0.7

2,4-Dimethyl-2-ethyl-1-pentanol

[66793-98-4]

C9H20O

MW = 144.26

147

C9H20O

MW = 144.26

148

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 298.15 52-doe/far 837.0 ± 1.5

2,4-Dimethyl-3-ethyl-3-pentanol

[3970-59-0]

Table 1. Fit with estimated B coefficient for 4 accepted points. Deviation σw = 0.542. Coefficient ρ = A + BT A 1081.51 B −0.760 cont.

Landolt-Börnstein New Series IV/8G

154

2.1.5 Alkanols, C9

2,4-Dimethyl-3-ethyl-3-pentanol (cont.) Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. ρexp − ρcalc Ref. ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 1) 273.15 877.3 ± 2.0 3.38 26-sta 293.15 858.8 ± 0.6 0.08 47-how/mea 293.15 860.8 ± 2.0 2.08 26-sta1) 298.15 854.3 ± 0.6 47-how/mea −0.62 303.15 853.2 ± 2.0 2.08 26-sta1) 293.15 858.8 ± 0.6 0.08 51-smi/cre 293.15 860.0 ± 1.0 1.28 43-geo 1)

Not included in calculation of linear coefficients.

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 290.00 861.1 ± 0.8 293.15 858.7 ± 0.7 298.15 854.9 ± 0.7 2,2-Dimethyl-3-heptanol

[19549-70-3]

C9H20O

MW = 144.26

149

C9H20O

MW = 144.26

150

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.020. Coefficient ρ = A + BT A 1050.33 B −0.760 Table 2. Experimental values with uncertainties and deviation from calculated values. T K

295.15 299.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m

kg ⋅ m−3

−3

826.0 ± 1.0 823.0 ± 1.0

Ref.

−0.02 0.02

49-col/lag 59-fol/wel

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 290.00 829.9 ± 1.1 293.15 827.5 ± 1.0 298.15 823.7 ± 0.9 2,3-Dimethyl-2-heptanol

[66794-00-1]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 48-naz/tor 839.6 ± 1.0

Landolt-Börnstein New Series IV/8G

2.1.5 Alkanols, C9 2,3-Dimethyl-3-heptanol

[19549-71-4]

155 C9H20O

MW = 144.26

151

[65822-93-7]

C9H20O

MW = 144.26

152

[19549-77-0]

C9H20O

MW = 144.26

153

Table 1. Experimental values with uncertainties. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 33-whi/eve 839.5 ± 2.0 294.15 33-whi/eve 838.3 ± 2.0 293.15 50-naz/bak 834.9 ± 3.0

2,4-Dimethyl-2-heptanol Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 298.15 59-col/gau 828.0 ± 1.0

2,4-Dimethyl-4-heptanol

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est ρexp ± 2σ est T T Ref. −3 K K kg ⋅ m kg ⋅ m−3 293.15 09-bod/tab 293.15 826.0 ± 1.0 824.2 ± 1.0 1) 293.15 33-mey/tuo 293.15 821.5 ± 3.0 824.2 ± 1.0 293.15 42-hen/all 293.15 825.4 ± 1.0 824.8 ± 1.0 293.15 54-naz/kak-3 824.2 ± 1.0 1)

Ref. 59-pet/zak 59-pet/zak-1 Recommended

Not included in calculation of recommended value.

2,5-Dimethyl-2-heptanol

[1561-18-8]

C9H20O

MW = 144.26

154

[13254-34-7]

C9H20O

MW = 144.26

155

C9H20O

MW = 144.26

156

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 295.15 31-lev/mar-2 830.0 ± 2.0

2,6-Dimethyl-2-heptanol

Table 1. Experimental values with uncertainties. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 26-pas/zam 818.6 ± 2.0 283.65 28-esc 816.2 ± 2.0

2,6-Dimethyl-3-heptanol

[19549-73-6]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 12-mic1) 821.2 ± 4.0 293.15 36-tuo 814.8 ± 2.0 293.15 Recommended 814.8 ± 2.0 1)

Not included in calculation of recommended value.

Landolt-Börnstein New Series IV/8G

156 2,6-Dimethyl-4-heptanol

2.1.5 Alkanols, C9 [108-82-7]

C9H20O

MW =144.26

157

Table 1. Fit with estimated B coefficient for 8 accepted points. Deviation σw = 0.427. Coefficient ρ = A + BT A 1033.02 B −0.760 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 ⋅ kg m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 294.15 809.0 ± 1.0 14-vav 333.15 779.9 ± 0.4 0.05 −0.47 293.15 811.4 ± 1.0 1.17 36-tuo 293.15 810.6 ± 1.0 0.37 293.15 809.7 ± 0.4 47-str/gab 293.15 0.47 −0.56 810.7 ± 1.0 313.15 795.2 ± 0.4 0.17 47-str/gab 293.15 810.7 ± 1.0 0.47 Table 3. Recommended values. ρexp ± 2σ est T T K K kg ⋅ m−3 290.00 310.00 812.6 ± 1.3 293.15 320.00 810.2 ± 1.1 298.15 806.4 ± 1.0 3,5-Dimethyl-3-heptanol

ρexp ± 2σ est kg ⋅ m

−3

797.4 ± 0.8 789.8 ± 1.0

T K 330.00 340.00

[19549-74-7]

Ref. 47-str/gab 53-ano-5 58-ano-5 68-ano

ρexp ± 2σ est kg ⋅ m−3

782.2 ± 1.3 774.6 ± 1.8

C9H20O

MW = 144.26

158

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 1.930. Coefficient ρ = A + BT A 1066.31 B −0.820 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc ρexp ± 2σ est T Ref. −3 kg ⋅ m−3 K kg ⋅ m 298.15 30-dav/dix1) 817.7 ± 3.0 −4.13 297.15 11.35 48-bro/bro1) 834.0 ± 8.0 301.15 11.63 48-bro/bro1) 831.0 ± 8.0 293.15 59-mac/bar 824.0 ± 2.0 −1.93 301.15 1.93 60-tha/vas 821.3 ± 2.0 1)

Not included in calculation of linear coefficients.

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 290.00 828.5 ± 2.1 293.15 825.9 ± 2.1 298.15 821.8 ± 2.1 310.00 812.1 ± 2.2

Landolt-Börnstein New Series IV/8G

2.1.5 Alkanols, C9 3,5-Dimethyl-4-heptanol

[19549-79-2]

157 C9H20O

MW = 144.26

159

C9H20O

MW = 144.26

160

C9H20O

MW = 144.26

161

C9H20O

MW = 144.26

162

C9H20O

MW = 144.26

163

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est

T K

291.15 293.15 293.15 1)

Ref.

−3

kg ⋅ m

836.0 ± 10.0 859.2 ± 1.0 859.2 ± 1.0

23-vav/iva1) 52-lev/shu Recommended

Not included in calculation of recommended value.

3,6-Dimethyl-1-heptanol

[1573-33-7]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 300.15 32-lev/mar 823.0 ± 2.0

3,6-Dimethyl-3-heptanol

[1573-28-0]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 289.15 04-kon 828.5 ± 2.0

4,6-Dimethyl-2-heptanol

[51079-52-8]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est

T K

273.15 273.15 298.15 298.15 1)

Ref.

kg ⋅ m

−3

878.7 ± 2.0 880.1 ± 2.0 822.0 ± 1.5 822.0 ± 1.5

09-gue1) 12-gue1) 64-hin/dre Recommended

Not included in calculation of recommended value.

5,6-Dimethyl-2-heptanol

[58795-24-7]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 291.15 11-wal 835.0 ± 2.0

Landolt-Börnstein New Series IV/8G

158

2.1.5 Alkanols, C9

6,6-Dimethyl-1-heptanol

[65769-10-0]

C9H20O

MW = 144.26

164

C9H20O

MW = 144.26

165

C9H20O

MW = 144.26

166

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 56-gol/kon 843.9 ± 1.0

3-Ethyl-1-heptanol

[3525-25-5]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 296.15 31-lev/mar-3 834.0 ± 2.0

3-Ethyl-3-heptanol

[19780-41-7]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 3.4886 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.4242 · 10−1 (combined temperature ranges, unweighted). T = 273.15 to 338.15 K ρ = A + BT + CT 2 + DT 3 + … 1.07793 · 103 −8.33559 · 10−1

Coefficient A B

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc Ref. (Symbol ρexp ± 2σ est ρexp ± 2σ est T T in Fig. 1) in Fig. 1) kg ⋅ m−3 kg ⋅ m−3 K K kg ⋅ m−3 kg ⋅ m−3 293.15 832.90 ± 1.00 −0.67 38-whi/ore( ) 318.15 812.60 ± 1.00 −0.14 39-owe/qua( ) 273.15 850.50 ± 1.00 0.25 39-owe/qua( ) 328.15 804.30 ± 1.00 −0.10 39-owe/qua( ) 298.15 829.90 ± 1.00 0.49 39-owe/qua( ) 338.15 796.30 ± 1.00 0.24 39-owe/qua( ) 308.15 821.00 ± 1.00 −0.07 39-owe/qua( )

Further references: [29-con/bla, 33-whi/woo]. Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15

ρ ± σ fit kg ⋅ m−3 852.87 ± 1.22 844.54 ± 1.13 836.20 ± 1.05 833.57 ± 1.04

T K

298.15 300.00 310.00 320.00

ρ ± σ fit kg ⋅ m−3 829.41 ± 1.02 827.86 ± 1.01 819.53 ± 1.00 811.19 ± 1.02

T K

330.00 340.00 350.00

ρ ± σ fit kg ⋅ m−3 802.86 ± 1.08 794.52 ± 1.16 786.19 ± 1.26

cont. Landolt-Börnstein New Series IV/8G

159

ρ

ρ

2.1.5 Alkanols, C9

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

5-Ethyl-1-heptanol

[998-65-2]

C9H20O

MW = 144.26

167

C9H20O

MW = 144.26

168

C9H20O

MW = 144.26

169

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 298.15 62-col/des 848.0 ± 1.0 2-Ethyl-3-methyl-1-hexanol

[66794-04-5]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 298.15 32-con/adk 835.8 ± 1.0 2-Ethyl-4-methyl-1-hexanol

[66794-06-7]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 58-hag/hud 828.8 ± 1.0

Landolt-Börnstein New Series IV/8G

160 2-Ethyl-5-methyl-1-hexanol

2.1.5 Alkanols, C9 [66794-07-8]

C9H20O

MW = 144.26

170

C9H20O

MW = 144.26

171

C9H20O

MW = 144.26

172

C9H20O

MW = 144.26

173

MW = 144.26

174

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 32-con/adk 820.8 ± 1.0

3-Ethyl-2-methyl-1-hexanol

[66794-01-2]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 295.15 54-naz/kak-41) 848.0 ± 2.0 293.15 54-naz/kak-4 851.2 ± 1.0 293.15 Recommended 851.2 ± 1.0 1)

Not included in calculation of recommended value.

3-Ethyl-2-methyl-2-hexanol

[66794-02-3]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 54-ski/flo 833.4 ± 1.0

3-Ethyl-2-methyl-3-hexanol

[66794-03-4]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 26-sta1) 850.6 ± 2.0 295.15 54-naz/kak-41) 845.2 ± 2.0 298.15 54-ski/flo 844.5 ± 1.0 298.15 Recommended 844.5 ± 1.0 1)

Not included in calculation of recommended value.

3-Ethyl-4-methyl-3-hexanol

[51200-80-7]

C9H20O

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 288.15 44-pre/zal 861.0 ± 1.0

Landolt-Börnstein New Series IV/8G

2.1.5 Alkanols, C9 3-Ethyl-5-methyl-3-hexanol

[597-77-3]

161 C9H20O

MW = 144.26

175

C9H20O

MW = 144.26

176

C9H20O

MW = 144.26

177

C9H20O

MW = 144.26

178

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 295.15 14-hal 839.6 ± 2.0

4-Ethyl-2-methyl-3-hexanol

[33943-21-4]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 43-geo 827.5 ± 1.0

4-Ethyl-3-methyl-3-hexanol

[66794-05-6]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 298.15 54-ski/flo 899.4 ± 1.0

1-Ethyl-1-propyl-1-butanol

[597-90-0]

Table 1. Fit with estimated B coefficient for 4 accepted points. Deviation σw = 0.464. Coefficient ρ = A + BT A 1074.08 B −0.820 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. ρexp − ρcalc Ref. ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 1) 289.15 838.4 ± 2.0 1.42 19-eyk 298.15 829.9 ± 1.0 0.30 39-owe/qua 293.15 833.7 ± 1.5 0.00 26-sta 328.15 804.3 ± 1.0 39-owe/qua −0.70 273.15 850.5 ± 1.0 0.40 39-owe/qua 293.15 836.4 ± 2.0 2.70 54-naz/kak-31) 1)

Not included in calculation of linear coefficients.

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 270.00 852.7 ± 1.9 280.00 844.5 ± 1.4 290.00 836.3 ± 1.0

Landolt-Börnstein New Series IV/8G

T K

293.15 298.15 310.00

ρexp ± 2σ est kg ⋅ m

−3

833.7 ± 0.9 829.6 ± 0.8 819.9 ± 1.1

T K

320.00 330.00

ρexp ± 2σ est kg ⋅ m−3

811.7 ± 1.5 803.5 ± 2.0

162 2-Methyl-1-octanol

2.1.5 Alkanols, C9 [818-81-5]

C9H20O

MW = 144.26

179

C9H20O

MW = 144.26

180

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 277.15 04-bou/bla-2 841.8 ± 1.0

2-Methyl-2-octanol

[628-44-4]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 1.2926 (combined temperature ranges, weighted), σc,uw = 8.1386 · 10−1 (combined temperature ranges, unweighted).

Coefficient A B

T = 273.15 to 338.15 K ρ = A + BT + CT 2 + DT 3 + … 1.05740 · 103 −8.13336 · 10−1

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 293.15 821.00 ± 2.00 2.02 38-whi/ore( ) 318.15 797.70 ± 1.00 −0.94 273.15 833.60 ± 1.00 −1.64 39-owe/qua( ) 328.15 789.70 ± 1.00 −0.81 298.15 813.40 ± 1.00 −1.51 39-owe/qua( ) 338.15 781.60 ± 1.00 −0.77 308.15 805.50 ± 1.00 −1.27 39-owe/qua( ) 293.15 823.90 ± 4.00 4.92

39-owe/qua( ) 39-owe/qua( ) 39-owe/qua( ) 56-tar/tai(∆)

ρ

ρ

Ref. (Symbol in Fig. 1)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont. Landolt-Börnstein New Series IV/8G

2.1.5 Alkanols, C9

163

Further references: [59-her]. Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ).

ρ ± σ fit kg ⋅ m−3

T K

T K

837.80 ± 2.47 829.67 ± 2.45 821.54 ± 2.42 818.98 ± 2.35

270.00 280.00 290.00 293.15

298.15 300.00 310.00 320.00

2-Methyl-3-octanol

ρ ± σ fit kg ⋅ m−3 814.91 ± 2.13 813.40 ± 2.02 805.27 ± 1.32 797.14 ± 0.75

[26533-34-6]

T K

330.00 340.00 350.00

ρ ± σ fit kg ⋅ m−3 789.00 ± 0.76 780.87 ± 1.60 772.74 ± 3.78

C9H20O

MW = 144.26

181

C9H20O

MW = 144.26

182

C9H20O

MW = 144.26

183

Table 1. Experimental and recommended values with uncertainties. T K 293.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

kg ⋅ m−3

827.0 ± 3.0 833.1 ± 2.0 833.1 ± 2.0

12-pic/ken1) 31-lev/mar-4 Recommended

Not included in calculation of recommended value.

2-Methyl-4-octanol

[40575-41-5]

Table 1. Experimental and recommended values with uncertainties. T K 293.15 293.15 298.15 298.15 1)

ρexp ± 2σ est

Ref.

kg ⋅ m−3

815.0 ± 3.0 813.0 ± 4.0 815.0 ± 2.0 815.0 ± 2.0

06-mal-11) 36-tuo1) 54-dub/luf Recommended

Not included in calculation of recommended value.

3-Methyl-1-octanol

[38514-02-2]

Table 1. Experimental values with uncertainties. ρexp ± 2σ est T Ref. K kg ⋅ m−3 297.15 31-lev/mar-1 827.0 ± 2.0 297.15 31-lev/mar-5 827.0 ± 2.0

Landolt-Börnstein New Series IV/8G

164

2.1.5 Alkanols, C9

3-Methyl-2-octanol

[27644-49-1]

C9H20O

MW = 144.26

184

[5340-36-3]

C9H20O

MW = 144.26

185

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 300.15

831.0 ± 2.0

33-pow/mur

3-Methyl-3-octanol

Table 1. Fit with estimated B coefficient for 6 accepted points. Deviation σw = 0.605.

ρ = A + BT

Coefficient A B

1072.01 −0.820

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 298.15 293.15 298.15 318.15 1)

825.8 ± 2.0 821.6 ± 8.0 827.5 ± 1.0 811.1 ± 1.0

−1.73 −10.03 −0.03 −0.03

33-whi/wil 34-gre1) 44-qua/sma 44-qua/sma

328.15 802.9 ± 1.0 293.15 833.1 ± 2.0 293.15 832.2 ± 2.0

−0.03 1.47 0.57

Ref. 44-qua/sma 54-pom/foo-1 61-sok/she

Not included in calculation of linear coefficients.

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 290.00 293.15

834.2 ± 2.5 831.6 ± 2.2

T K 298.15 310.00

3-Methyl-4-octanol

ρexp ± 2σ est kg ⋅ m−3

827.5 ± 1.8 817.8 ± 1.3

T K 320.00 330.00

ρexp ± 2σ est kg ⋅ m−3

809.6 ± 1.6 801.4 ± 2.3

[26533-35-7]

C9H20O

MW = 144.26

186

[38514-03-3]

C9H20O

MW = 144.26

187

[66793-80-4]

C9H20O

MW = 144.26

188

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 291.15

834.0 ± 2.0

23-vav/iva

4-Methyl-1-octanol Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 300.65 31-lev/mar-5 820.0 ± 2.0

4-Methyl-3-octanol Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 298.15 843.7 ± 2.0 34-gre

Landolt-Börnstein New Series IV/8G

2.1.5 Alkanols, C9 4-Methyl-4-octanol

[23418-37-3]

165 C9H20O

MW = 144.26

189

Table 1. Fit with estimated B coefficient for 4 accepted points. Deviation σw = 0.328. Coefficient ρ = A + BT A 1069.04 B −0.820 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 ⋅ kg m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 293.15 826.7 ± 2.0 33-whi/woo1) 328.15 799.9 ± 1.0 −1.96 −0.06 298.15 823.7 ± 2.0 33-whi/woo1) 293.15 828.4 ± 0.6 −0.86 −0.26 298.15 825.2 ± 1.0 0.64 44-qua/sma 293.15 822.7 ± 4.0 −5.96 318.15 808.3 ± 1.0 0.14 44-qua/sma 1)

Ref. 44-qua/sma 54-pom/foo-1 59-yur/bel-11)

Not included in calculation of linear coefficients.

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 290.00 831.2 ± 0.9 293.15 828.7 ± 0.8

5-Methyl-1-octanol

ρexp ± 2σ est

T K 298.15 310.00

kg ⋅ m

−3

824.6 ± 0.6 814.8 ± 0.6

[38514-04-4]

T K 320.00 330.00

ρexp ± 2σ est kg ⋅ m−3

806.6 ± 1.0 798.4 ± 1.4

C9H20O

MW = 144.26

190

C9H20O

MW = 144.26

191

C9H20O

MW = 144.26

192

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 297.15 33-lev/mar-1 828.0 ± 2.0

5-Methyl-2-octanol

[66793-81-5]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 298.15 31-lev/mar-4 821.0 ± 2.0

5-Methyl-4-octanol

[59734-23-5]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 298.15 12-bje 815.6 ± 0.8

Landolt-Börnstein New Series IV/8G

166 (S)-6-Methyl-1-octanol

2.1.5 Alkanols, C9 [110453-78-6]

C9H20O

MW = 144.26

193

C9H20O

MW = 144.26

194

C9H20O

MW = 144.26

195

C9H20O

MW = 144.26

196

C9H20O

MW = 144.26

197

C9H20O

MW = 144.26

198

C9H20O

MW = 144.26

199

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 297.15 33-lev/mar-1 828.0 ± 2.0 6-Methyl-3-octanol

[40225-75-0]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 301.15 36 -pow/bal -0 832.0 ± 1.0 6-Methyl-4-octanol

[66793-82-6]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 296.15 31-lev/mar-4 822.0 ± 2.0 7-Methyl-1-octanol

[2430-22-0]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 16-lev/all 826.0 ± 2.0 7-Methyl-3-octanol

[66793-84-8]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 285.15 25-tho/kah 840.2 ± 2.0 7-Methyl-4-octanol

[33933-77-6]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 36-tuo 813.6 ± 1.0 4-Methyl-2-propyl-1-pentanol

[54004-41-0]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 58-hag/hud 825.6 ± 1.0

Landolt-Börnstein New Series IV/8G

2.1.5 Alkanols, C9 1-Nonanol

[143-08-8]

Tc = 670.50 K [89-tej/lee]

167 C9H20O

MW = 144.26

200

ρc = 264.00 kg·m−3 [89-tej/lee]

Table 1. Coefficients for the polynomial expansion equations. Standard deviations (see introduction): σ = 9.8705 · 10−1 (low temperature range), σc,w = (5.4570 · 10−1 combined temperature ranges, weighted), σc,uw = 4.0529 · 10−1 (combined temperature ranges, unweighted).

Coefficient

T = 273.15 to 540.00 K ρ = A + BT + CT 2 + DT 3 + …

9.49744 · 102 −7.07347 · 10−2 −1.43841 · 10−3 8.99651 · 10−7

A B C D

T = 540.00 to 670.50 K ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)] [ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] 2.41155 −5.85206 · 10−2 5.31779 · 10−4 −1.62241 · 10−6

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) ⋅ kg m kg ⋅ m−3 K K ⋅ ⋅ kg m kg m 273.15 841.50 ± 1.00 0.06 1886-kra(✕ ) 288.15 831.00 ± 1.70 −0.45 273.15 841.50 ± 0.60 0.06 1886-kra(✕ ) 288.45 831.00 ± 1.70 −0.25 283.15 834.60 ± 0.60 −0.22 1886-kra(✕ ) 293.15 827.80 ± 1.70 −0.26 283.15 834.60 ± 1.00 −0.22 1886-kra1) 298.85 822.30 ± 1.60 −1.85 293.15 827.90 ± 0.60 −0.16 1886-kra1) 298.95 822.30 ± 1.60 −1.78 1) 293.15 827.90 ± 1.00 −0.16 1886-kra 303.15 821.80 ± 1.60 0.63 273.15 840.00 ± 0.30 −1.44 313.15 815.50 ± 1.60 1.33 32-ell/rei(∇) 298.15 823.01 ± 0.30 −1.62 322.85 809.50 ± 1.60 2.25 32-ell/rei(∇) 273.15 827.00 ± 1.50 −14.44 66-efr1) 323.15 809.20 ± 1.60 2.16 293.15 827.00 ± 1.50 −1.06 66-efr1) 323.45 809.10 ± 1.60 2.28 313.15 813.00 ± 1.50 −1.17 66-efr1) 333.15 802.80 ± 1.60 3.00 333.15 800.00 ± 1.50 0.20 66-efr1) 343.15 796.10 ± 1.60 3.65 353.15 786.00 ± 1.50 1.00 66-efr1) 347.75 793.20 ± 1.60 4.17 373.15 771.00 ± 1.50 1.19 66-efr1) 347.75 793.10 ± 1.60 4.07 393.15 755.00 ± 1.50 0.73 66-efr(✕ ) 347.85 792.90 ± 1.60 3.94 413.15 739.00 ± 1.50 0.56 66-efr(✕ ) 353.15 789.20 ± 1.60 4.20 433.15 722.00 ± 1.50 −0.34 66-efr(✕ ) 363.15 782.20 ± 1.60 4.75 453.15 704.00 ± 1.50 −2.03 66-efr(✕ ) 369.95 777.50 ± 1.60 5.24 473.15 686.00 ± 1.50 −3.55 66-efr(✕ ) 370.25 777.20 ± 1.60 5.17 493.15 667.00 ± 1.50 −5.94 66-efr(✕ ) 370.35 776.80 ± 1.60 4.84 513.15 648.00 ± 1.50 −8.24 66-efr(✕ ) 373.15 775.00 ± 1.60 5.19 533.15 629.00 ± 1.50 −10.50 66-efr1) 383.15 767.10 ± 1.50 5.02 553.15 607.00 ± 1.50 −10.86 66-efr(✕ ) 393.15 759.40 ± 1.50 5.13 573.15 585.00 ± 1.50 −1.41 66-efr(✕ ) 403.15 751.20 ± 1.50 4.81 593.15 560.00 ± 1.50 0.90 66-efr(✕ ) 413.15 742.80 ± 1.50 4.36 613.15 541.00 ± 1.50 4.05 66-efr(✕ ) 423.15 734.10 ± 1.50 3.68 633.15 500.00 ± 2.00 −7.88 66-efr(✕ ) 424.35 733.20 ± 1.50 3.75 653.15 450.00 ± 2.00 2.95 66-efr(✕ ) 424.75 732.80 ± 1.50 3.67 663.15 420.00 ± 3.00 30.57 66-efr1) 424.85 732.30 ± 1.50 3.25 1)

Ref. (Symbol in Fig. 1) 71-gol/dob1) 71-gol/dob1) 71-gol/dob1) 71-gol/dob1) 71-gol/dob1) 71-gol/dob1) 71-gol/dob1) 71-gol/dob1) 71-gol/dob1) 71-gol/dob1) 71-gol/dob1) 71-gol/dob1) 71-gol/dob1) 71-gol/dob1) 71-gol/dob1) 71-gol/dob1) 71-gol/dob1) 71-gol/dob1) 71-gol/dob1) 71-gol/dob1) 71-gol/dob1) 71-gol/dob(✕ ) 71-gol/dob(✕ ) 71-gol/dob(✕ ) 71-gol/dob(✕ ) 71-gol/dob(✕ ) 71-gol/dob(✕ ) 71-gol/dob(✕ ) 71-gol/dob(✕ )

Not included in Fig. 1.

cont. Landolt-Börnstein New Series IV/8G

168

2.1.5 Alkanols, C9

1-Nonanol (cont.) Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 433.15 725.00 ± 1.50 2.66 71-gol/dob(✕ ) 298.15 824.60 ± 0.30 −0.03 443.15 715.50 ± 1.40 1.29 71-gol/dob(✕ ) 303.15 821.60 ± 0.30 0.43 453.15 705.80 ± 1.40 −0.23 71-gol/dob(✕ ) 308.15 818.10 ± 0.30 0.41 463.15 695.00 ± 1.40 −2.81 71-gol/dob(✕ ) 313.15 814.70 ± 0.30 0.53 473.15 685.00 ± 1.40 −4.55 71-gol/dob(✕ ) 318.15 811.00 ± 0.30 0.38 473.15 685.80 ± 1.40 −3.75 71-gol/dob(✕ ) 288.15 831.00 ± 0.40 −0.45 474.45 683.10 ± 1.40 −5.38 71-gol/dob(✕ ) 298.15 824.40 ± 0.40 −0.23 483.15 673.60 ± 1.30 −7.66 71-gol/dob1) 308.15 817.70 ± 0.40 0.01 300.45 823.39 ± 0.40 0.34 73-nay/kud1) 318.15 811.10 ± 0.50 0.48 310.27 816.77 ± 0.40 0.57 73-nay/kud(✕ ) 328.15 804.30 ± 0.50 0.87 320.89 809.11 ± 0.40 0.45 73-nay/kud(✕ ) 298.15 824.72 ± 0.20 0.09 330.83 802.40 ± 0.40 0.91 73-nay/kud1) 323.15 806.92 ± 0.10 −0.12 340.81 794.57 ± 0.40 0.39 73-nay/kud1) 328.15 803.98 ± 0.10 0.55 350.02 788.06 ± 0.40 0.72 73-nay/kud1) 333.15 799.70 ± 0.10 −0.10 359.78 780.30 ± 0.40 0.30 73-nay/kud1) 338.15 796.32 ± 0.10 0.19 369.70 772.24 ± 0.40 −0.21 73-nay/kud(✕ ) 343.15 792.34 ± 0.10 −0.11 293.15 828.10 ± 0.30 0.04 348.15 788.36 ± 0.10 −0.37 76-hon/sin(∆) 298.15 824.47 ± 0.20 −0.16 79-dia/tar( ) 353.15 785.08 ± 0.10 0.08 308.15 817.58 ± 0.20 −0.11 79-dia/tar( ) 358.15 781.10 ± 0.10 −0.13 318.15 810.62 ± 0.20 0.00 79-dia/tar( ) 363.15 777.09 ± 0.10 −0.36 333.15 799.91 ± 0.20 0.11 79-dia/tar( ) 373.15 769.58 ± 0.10 −0.23 293.15 827.70 ± 0.30 −0.36 82-ort(◆)

1)

Ref. (Symbol in Fig. 1) 82-ort(◆) 82-ort(◆) 82-ort(◆) 82-ort(◆) 82-ort(◆) 83-rau/ste(✕ ) 83-rau/ste1) 83-rau/ste1) 83-rau/ste1) 83-rau/ste1) 85-fer/pin( ) 93-gar/ban-1(✕ ) 93-gar/ban-1(✕ ) 93-gar/ban-1(✕ ) 93-gar/ban-1(✕ ) 93-gar/ban-1(✕ ) 93-gar/ban-1(✕ ) 93-gar/ban-1(✕ ) 93-gar/ban-1(✕ ) 93-gar/ban-1(✕ ) 93-gar/ban-1(✕ )

Not included in Fig. 1.

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K 270.00 280.00 290.00 293.15 298.15 300.00 310.00 320.00 330.00 340.00 350.00 360.00 370.00 380.00 390.00

ρ ± σ fit kg ⋅ m−3 843.49 ± 0.59 836.92 ± 0.45 830.20 ± 0.35 828.06 ± 0.33 824.63 ± 0.30 823.36 ± 0.29 816.39 ± 0.26 809.30 ± 0.26 802.09 ± 0.29 794.77 ± 0.33 787.35 ± 0.40 779.84 ± 0.49 772.22 ± 0.59 764.52 ± 0.70 756.74 ± 0.82

T K 400.00 410.00 420.00 430.00 440.00 450.00 460.00 470.00 480.00 490.00 500.00 510.00 520.00 530.00 540.00

ρ ± σ fit kg ⋅ m−3 748.88 ± 0.95 740.95 ± 1.08 732.95 ± 1.21 724.89 ± 1.34 716.78 ± 1.46 708.62 ± 1.58 700.41 ± 1.69 692.16 ± 1.79 683.88 ± 1.88 675.56 ± 1.96 667.23 ± 2.03 658.88 ± 2.09 650.51 ± 2.14 642.14 ± 2.40 633.77 ± 2.76

T K 550.00 560.00 570.00 580.00 590.00 600.00 610.00 620.00 630.00 640.00 650.00 660.00 670.00

ρ ± σ fit kg ⋅ m−3 622.37 ± 3.08 607.28 ± 3.32 591.31 ± 3.56 576.25 ± 3.71 562.92 ± 3.96 551.28 ± 4.23 540.44 ± 4.41 528.74 ± 4.61 513.76 ± 4.83 492.33 ± 5.29 460.27 ± 5.49 410.90 ± 6.75 307.42 ± 8.10

cont. Landolt-Börnstein New Series IV/8G

2.1.5 Alkanols, C9

169

ρ

ρ

Further references: [00-ste, 19-beh, 27-ver/coo, 29-mah/das, 33-ano, 37-oli, 42-mul, 48-vog-2, 50-sac/sau, 52-coo, 52-eri-1, 57-gol/kon, 81-sjo/dyh, 85-ort/paz-1, 88-ort/gar, 90-klo/pal, 93-ami/rai, 93-yan/mae, 94-yu /tsa-1].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

2-Nonanol

[628-99-9]

C9H20O

MW = 144.26

201

Table 1. Fit with estimated B coefficient for 4 accepted points. Deviation σw = 0.974. Coefficient ρ = A + BT A 1045.94 B −0.760 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 1) 293.15 847.1 ± 20.0 23.93 06-van 403.15 730.4 ± 3.0 −9.15 273.15 839.9 ± 1.0 1.55 09-mas 273.15 837.2 ± 1.0 −1.14 298.15 823.0 ± 4.0 3.65 10-hal/las1) 298.15 819.1 ± 1.0 −0.27 293.15 823.0 ± 1.0 11-pic/ken −0.15 1)

Ref. 12-pic/ken1) 32-ell/rei 32-ell/rei

Not included in calculation of linear coefficients.

cont. Landolt-Börnstein New Series IV/8G

170

2.1.5 Alkanols, C9

2-Nonanol (cont.) Table 3. Recommended values. ρexp ± 2σ est T T −3 K K kg ⋅ m 270.00 293.15 840.7 ± 1.8 280.00 298.15 833.1 ± 1.2 290.00 825.5 ± 1.2 3-Nonanol

ρexp ± 2σ est kg ⋅ m−3

823.1 ± 1.4 819.3 ± 1.8

[624-51-1]

C9H20O

MW = 144.26

202

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 1.150. Coefficient ρ = A + BT A 1068.03 B −0.820 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc ρexp ± 2σ est T Ref. −3 −3 kg ⋅ m K kg ⋅ m 293.15 13-pic/ken 826.5 ± 2.0 −1.15 353.15 1.15 13-pic/ken 779.6 ± 2.0 293.15 36-tuo1) 819.6 ± 4.0 −8.05 1)

Not included in calculation of linear coefficients.

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 290.00 830.2 ± 2.9 293.15 827.6 ± 2.7 298.15 823.5 ± 2.4 4-Nonanol

ρexp ± 2σ est

T K 310.00 320.00 330.00

kg ⋅ m

−3

813.8 ± 1.9 805.6 ± 1.7 797.4 ± 1.7 [5932-79-6]

T K 340.00 350.00 360.00

ρexp ± 2σ est kg ⋅ m−3

789.2 ± 2.0 781.0 ± 2.5 772.8 ± 3.1

C9H20O

MW = 144.26

203

C9H20O

MW = 144.26

204

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 57-shu/bel 826.3 ± 1.0 5-nonanol

[623-93-8]

Table 1. Fit with estimated B coefficient for 4 accepted points. Deviation σw = 0.293. Coefficient ρ = A + BT A 1044.87 B −0.760 cont.

Landolt-Börnstein New Series IV/8G

2.1.5 Alkanols, C9

171

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. ρexp − ρcalc Ref. ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 293.15 823.0 ± 1.0 0.92 06-mal-1 293.15 825.7 ± 2.0 3.62 47-tuo/guy1) 1) 289.15 824.4 ± 2.0 19-eyk 293.15 822.0 ± 0.4 50-mea/foo −0.72 −0.08 291.15 823.0 ± 1.0 23-vav/iva 298.15 818.3 ± 0.4 0.02 50-mea/foo −0.60 293.65 835.6 ± 10.0 13.90 42-boe/han1) 1)

Not included in calculation of linear coefficients.

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 290.00 824.5 ± 0.5 293.15 822.1 ± 0.5 298.15 818.3 ± 0.5

2,2,3,4-Tetramethyl-3-pentanol

[29772-39-2]

C9H20O

MW = 144.26

205

Table 1. Fit with estimated B coefficient for 5 accepted points. Deviation σw = 0.468. Coefficient ρ = A + BT A 1096.61 B −0.820

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. ρexp − ρcalc Ref. ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 293.15 856.4 ± 1.0 0.18 29-con/bla 293.15 856.5 ± 0.6 0.28 47-how/mea 293.15 856.0 ± 1.0 33-whi/lau 298.15 852.3 ± 0.6 0.18 47-how/mea −0.22 288.15 862.2 ± 2.0 1.88 36-naz1) 293.15 855.0 ± 1.0 48-cad/foo −1.22 1)

Not included in calculation of linear coefficients.

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 290.00 858.8 ± 0.8 293.15 856.2 ± 0.8 298.15 852.1 ± 0.8

Landolt-Börnstein New Series IV/8G

172

2.1.5 Alkanols, C9

2,2,3-Trimethyl-3-hexanol

[5340-41-0]

C9H20O

MW = 144.26

206

C9H20O

MW = 144.26

207

C9H20O

MW = 144.26

208

C9H20O

MW = 144.26

209

Table 1. Experimental and recommended values with uncertainties. T K

293.15 293.15 293.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

846.4 ± 1.0 848.5 ± 2.0 846.3 ± 1.0 846.0 ± 1.0 846.2 ± 1.0

43-geo 48-ruo1) 55-pet/sus 61-mar/pet Recommended

Not included in calculation of recommended value.

2,3,4-Trimethyl-2-hexanol

[21102-13-6]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 288.15 35-col-1 835.3 ± 1.0

2,3,5-Trimethyl-3-hexanol

[65927-60-8]

Table 1. Experimental and recommended values with uncertainties. T K

293.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

kg ⋅ m

−3

825.6 ± 3.0 831.2 ± 2.0 831.2 ± 2.0

33-mey/tuo1) 59-pet/zak-1 Recommended

Not included in calculation of recommended value.

2,4,4-Trimethyl-2-hexanol

[66793-91-7]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 40-mos 847.5 ± 1.0

Landolt-Börnstein New Series IV/8G

2.1.5 Alkanols, C9 2,4,4-Trimethyl-3-hexanol

[66793-92-8]

173 C9H20O

MW = 144.26

210

C9H20O

MW = 144.26

211

C9H20O

MW = 144.26

212

C9H20O

MW = 144.26

213

C9H20O

MW = 144.26

214

C9H20O

MW = 144.26

215

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 48-ruo 848.8 ± 1.0

2,5,5-Trimethyl-3-hexanol

[66793-72-4]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 42-whi/for 825.0 ± 1.0

3,4,4-Trimethyl-3-hexanol

[66793-74-6]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 294.15 06-kon/mil 832.3 ± 2.0

3,5,5-Trimethyl-1-hexanol

[3452-97-9]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 298.15 49-bru 823.6 ± 1.0

3,5,5-Trimethyl-3-hexanol

[66810-87-5]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 47-how/mea 835.0 ± 0.5

4,5,5-Trimethyl-1-hexanol

[66793-75-7]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 61-mar/pet 846.0 ± 1.0

Landolt-Börnstein New Series IV/8G

2.1.6 Alkanols, C10

175

2.1.6 Alkanols, C10 2-Butyl-1-hexanol

[2768-15-2]

C10H22O

MW = 158.28

216

C10H22O

MW = 158.28

217

Table 1. Experimental value with uncertainty. T K 289.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

836.0 ± 3.0

16-lev/all

1-Decanol

[112-30-1]

Tc = 687.10 K [89-tej/lee]

ρc = 264.00 kg·m−3 [89-tej/lee]

Table 1. Coefficients for the polynomial expansion equations. Standard deviations (see introduction): σ = 4.3461 · 10−1 (low temperature range), σc,w = (2.6342 · 10−1 combined temperature ranges, weighted), σc,uw = 3.3635 · 10−1 (combined temperature ranges, unweighted).

T = 279.63 to 550.00 K ρ = A + BT + CT 2 + DT 3 + …

Coefficient

1.01735 · 103 −6.79957 · 10−1 3.98783 · 10−4 −8.88242 · 10−7

A B C D

T = 550.00 to 687.10 K ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)] [ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] 1.30964 −1.59285 · 10−2 5.30923 · 10−5 7.66905 · 10−9

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 280.15 293.15 371.85 293.10 298.10 303.10 313.10 323.10 333.10 343.10 353.10 358.10 293.15 313.15 333.15 353.15 373.15 393.15 1)

ρexp ± 2σ est −3

kg ⋅ m

838.90 ± 1.00 829.70 ± 1.00 773.40 ± 1.00 830.10 ± 0.29 826.90 ± 0.30 823.50 ± 0.30 816.80 ± 0.32 810.00 ± 0.34 802.70 ± 0.36 795.40 ± 0.38 788.10 ± 0.39 784.20 ± 0.40 826.00 ± 0.52 812.70 ± 0.54 799.80 ± 0.56 785.80 ± 0.58 770.50 ± 0.60 755.00 ± 0.62

ρexp − ρcalc kg ⋅ m−3

0.27 −0.22 −0.58 0.15 0.33 0.34 0.51 0.67 0.42 0.27 0.22 −0.01 −3.92 −3.55 −2.44 −2.04 −2.50 −2.69

T K 1883-kra1) 413.15 1883-kra1) 433.15 1883-kra(✕ ) 453.15 55-kus1) 473.15 55-kus1) 493.15 55-kus1) 513.15 55-kus1) 533.15 55-kus1) 553.15 55-kus1) 293.15 55-kus(✕ ) 313.15 55-kus(✕ ) 333.15 55-kus(✕ ) 353.15 58-cos/bow1) 373.15 58-cos/bow1) 393.15 58-cos/bow1) 413.15 1) 58-cos/bow 433.15 58-cos/bow(✕ ) 453.15 58-cos/bow(✕ ) 473.15

Ref. (Symbol in Fig. 1)

ρexp ± 2σ est −3

kg ⋅ m

738.70 ± 0.64 722.40 ± 0.66 705.30 ± 0.68 688.30 ± 0.70 670.80 ± 0.72 653.50 ± 1.00 635.00 ± 1.00 612.70 ± 1.00 829.70 ± 1.50 816.20 ± 1.50 802.20 ± 1.50 787.60 ± 1.50 772.40 ± 1.50 757.20 ± 1.50 741.40 ± 1.50 727.50 ± 1.50 707.20 ± 1.50 694.00 ± 1.50

ρexp − ρcalc kg ⋅ m−3

−3.16 −3.06 −3.17 −2.52 −1.69 0.08 1.42 −0.35 −0.22 −0.05 −0.04 −0.24 −0.60 −0.49 −0.46 2.04 −1.27 3.18

Ref. (Symbol in Fig. 1) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr1) 66-efr(✕ ) 66-efr(✕ ) 66-efr1) 66-efr1) 66-efr1)

Not included in Fig. 1.

cont. Landolt-Börnstein New Series IV/8G

176

2.1.6 Alkanols, C10

1-Decanol (cont.) Table 2. Experimental values with uncertainties and deviation from calculated values. T K

493.15 513.15 533.15 553.15 573.15 593.15 613.15 633.15 653.15 673.15 279.63 279.85 281.69 286.12 286.15 293.15 293.16 303.14 313.13 313.15 323.08 323.09 333.14 333.16 293.15 298.15 303.15 308.15 298.15 308.15 318.15 333.15 298.15 298.15 298.15 283.15 298.15 313.15 293.15 298.15 333.15 298.15 298.15 1)

ρexp ± 2σ est −3

kg ⋅ m

675.00 ± 1.50 659.00 ± 1.50 643.00 ± 1.50 624.00 ± 1.50 605.00 ± 1.50 584.00 ± 1.50 564.00 ± 1.50 530.00 ± 2.00 496.00 ± 2.00 450.00 ± 3.00 838.86 ± 0.17 838.77 ± 0.17 837.53 ± 0.17 834.51 ± 0.17 834.45 ± 0.17 829.73 ± 0.17 829.73 ± 0.17 822.94 ± 0.16 816.07 ± 0.16 816.06 ± 0.16 809.17 ± 0.16 809.15 ± 0.16 802.07 ± 0.16 802.04 ± 0.16 829.69 ± 0.10 826.40 ± 0.10 823.04 ± 0.10 819.61 ± 0.10 826.23 ± 0.20 819.46 ± 0.20 812.58 ± 0.20 802.03 ± 0.20 826.57 ± 0.02 826.53 ± 0.02 826.57 ± 0.10 836.51 ± 0.20 826.40 ± 0.20 816.11 ± 0.20 829.82 ± 0.25 826.44 ± 0.25 802.02 ± 0.25 826.60 ± 0.33 826.80 ± 0.50

Not included in Fig. 1.

ρexp − ρcalc −3

kg ⋅ m

2.51 5.58 9.42 10.95 7.91 0.66 −1.22 −6.50 5.35 33.09 −0.12 −0.06 −0.08 −0.13 −0.17 −0.19 −0.18 −0.19 −0.20 −0.19 −0.17 −0.19 −0.18 −0.20 −0.23 −0.13 −0.09 −0.09 −0.30 −0.24 −0.21 −0.21 0.04 −0.00 0.04 −0.12 −0.13 −0.14 −0.10 −0.09 −0.22 0.07 0.27

Ref. (Symbol in Fig. 1) 1)

66-efr 66-efr(✕ ) 66-efr1) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr(✕ ) 66-efr1) 73-fin(∇) 73-fin(∇) 73-fin(∇) 73-fin(∇) 73-fin(∇) 73-fin1) 73-fin1) 73-fin1) 73-fin(∇) 73-fin(∇) 73-fin(∇) 73-fin(∇) 73-fin(∇) 73-fin(∇) 78-jel/leo(∆) 78-jel/leo(∆) 78-jel/leo(∆) 78-jel/leo(∆) 79-dia/tar1) 79-dia/tar1) 79-dia/tar(◆) 79-dia/tar(◆) 79-kiy/ben(✕ ) 81-ben/han( ) 85-kum/ben( ) 86-hei/sch(✕ ) 86-hei/sch1) 86-hei/sch(✕ ) 86-wag/hei1) 86-wag/hei1) 86-wag/hei(✕ ) 89-mat/mak-11) 89-mat/mak-11)

T K

303.15 308.15 313.15 318.15 323.15 323.15 328.15 333.15 338.15 343.15 348.15 348.15 283.15 293.15 303.15 323.15 343.15 363.15 383.15 403.15 423.15 433.15 443.15 453.15 463.15 473.15 483.15 493.15 288.15 293.15 298.15 303.15 308.15 313.15 318.15 323.15 328.15 333.15 338.15 343.15 348.15 353.15

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

823.20 ± 0.33 819.70 ± 0.33 816.30 ± 0.33 812.80 ± 0.33 809.30 ± 0.32 809.40 ± 0.49 805.90 ± 0.32 802.30 ± 0.32 798.70 ± 0.32 795.10 ± 0.32 791.50 ± 0.47 791.40 ± 0.32 834.30 ± 0.83 828.40 ± 0.83 822.60 ± 0.82 811.10 ± 0.81 798.20 ± 0.80 784.10 ± 0.78 769.40 ± 0.77 753.50 ± 0.75 737.20 ± 0.74 728.00 ± 0.73 719.20 ± 0.72 710.10 ± 0.71 700.60 ± 0.70 690.10 ± 0.69 679.60 ± 0.68 669.10 ± 0.67 833.90 ± 0.60 830.20 ± 0.60 827.00 ± 0.60 823.70 ± 0.60 820.10 ± 0.60 816.40 ± 0.60 812.90 ± 0.60 809.50 ± 0.60 805.80 ± 0.60 802.40 ± 0.60 798.80 ± 0.60 795.20 ± 0.60 791.60 ± 0.60 788.00 ± 0.60

0.07 −0.00 0.05 0.01 0.01 0.11 0.12 0.06 0.02 0.01 0.02 −0.08 −2.33 −1.52 −0.53 1.81 3.11 3.62 3.99 3.66 3.47 2.54 2.16 1.63 0.87 −0.72 −2.14 −3.39 0.62 0.28 0.47 0.57 0.40 0.15 0.11 0.21 0.02 0.16 0.12 0.11 0.12 0.16

kg ⋅ m

Ref. (Symbol in Fig. 1) 89-mat/mak-11) 89-mat/mak-11) 89-mat/mak-11) 89-mat/mak-11) 89-mat/mak-11) 89-mat/mak-11) 89-mat/mak-11) 89-mat/mak-11) 89-mat/mak-1(✕ ) 89-mat/mak-1(✕ ) 89-mat/mak-1(✕ ) 89-mat/mak-1(✕ ) 90-apa/gyl1) 90-apa/gyl1) 90-apa/gyl1) 90-apa/gyl1) 90-apa/gyl1) 90-apa/gyl(✕ ) 90-apa/gyl(✕ ) 90-apa/gyl(✕ ) 90-apa/gyl(✕ ) 90-apa/gyl(✕ ) 90-apa/gyl(✕ ) 90-apa/gyl(✕ ) 90-apa/gyl(✕ ) 90-apa/gyl(✕ ) 90-apa/gyl(✕ ) 90-apa/gyl(✕ ) 92-lie/sen-11) 92-lie/sen-11) 92-lie/sen-11) 92-lie/sen-11) 92-lie/sen-11) 92-lie/sen-11) 92-lie/sen-11) 92-lie/sen-11) 92-lie/sen-11) 92-lie/sen-11) 92-lie/sen-11) 92-lie/sen-11) 92-lie/sen-11) 92-lie/sen-1(✕ ) cont.

Landolt-Börnstein New Series IV/8G

177

ρ

ρ

2.1.6 Alkanols, C10

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15 300.00 310.00 320.00 330.00 340.00 350.00 360.00 370.00 380.00 390.00

ρ ± σ fit kg ⋅ m−3 845.35 ± 0.11 838.73 ± 0.11 832.04 ± 0.14 829.92 ± 0.16 826.53 ± 0.18 825.27 ± 0.19 818.43 ± 0.23 811.50 ± 0.28 804.47 ± 0.32 797.36 ± 0.37 790.14 ± 0.41 782.81 ± 0.46 775.37 ± 0.51 767.81 ± 0.55 760.14 ± 0.60

T K

400.00 410.00 420.00 430.00 440.00 450.00 460.00 470.00 480.00 490.00 500.00 510.00 520.00 530.00 540.00

ρ ± σ fit kg ⋅ m−3 752.33 ± 0.64 744.39 ± 0.69 736.31 ± 0.74 728.09 ± 0.78 719.71 ± 0.82 711.19 ± 0.87 702.50 ± 0.91 693.64 ± 0.95 684.62 ± 1.00 675.42 ± 1.05 666.04 ± 1.11 656.47 ± 1.17 646.71 ± 1.25 636.76 ± 1.34 626.60 ± 1.85

T K

550.00 560.00 570.00 580.00 590.00 600.00 610.00 620.00 630.00 640.00 650.00 660.00 670.00 680.00

ρ ± σ fit kg ⋅ m−3 616.23 ± 2.38 606.90 ± 2.49 599.28 ± 2.54 592.47 ± 2.60 585.63 ± 2.76 577.94 ± 2.84 568.62 ± 2.94 556.89 ± 3.16 541.98 ± 3.30 523.10 ± 3.79 499.33 ± 4.03 469.47 ± 4.35 431.35 ± 5.79 378.50 ± 6.41 cont.

Landolt-Börnstein New Series IV/8G

178

2.1.6 Alkanols, C10

1-Decanol (cont.) Further references: [09-sch-1, 27-ver/coo, 48-jon/bow, 48-vog-2, 48-wei, 50-sac/sau, 56-rat/cur, 68-pfl/pop, 68-sin/ben, 69-smi/kur, 78-ast, 78-tre/ben, 81-kiy/ben, 81-sjo/dyh, 81-tre/kiy, 82-ort, 82-tre/han, 83-gop/rao, 83-rau/ste, 84-kum/ben, 85-fer/pin, 85-ort/paz-1, 86-dew/meh, 87-dew/meh, 88-ort/gar, 89-dew/gup, 93-yan/mae, 94-yu /tsa-1]. 2-Decanol

[1120-06-5]

C10H22O

MW = 158.28

218

MW = 158.28

219

Table 1. Experimental and recommended values with uncertainties. T K 293.15 293.15 293.15 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

825.0 ± 1.0 824.9 ± 1.0 825.6 ± 1.0 825.2 ± 1.0

11-pic/ken 59-asi/gei 60-kor/pet Recommended

3-Decanol

[1565-81-7]

C10H22O

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 0.283. Coefficient ρ = A + BT 1055.46 A B −0.780 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

293.15 353.15 293.15

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−3

kg ⋅ m

827.2 ± 1.0 779.8 ± 1.0 826.6 ± 1.0

0.40 −0.20 −0.20

13-pic/ken 13-pic/ken 59-asi/gei

Table 3. Recommended values. ρexp ± 2σ est

T K

T K

−3

kg ⋅ m

829.3 ± 1.5 826.8 ± 1.4 822.9 ± 1.2

290.00 293.15 298.15

310.00 320.00 330.00

4-Decanol

ρexp ± 2σ est

T K

−3

kg ⋅ m

813.7 ± 1.0 805.9 ± 1.0 798.1 ± 1.3 [2051-31-2]

340.00 350.00 360.00 C10H22O

ρexp ± 2σ est kg ⋅ m−3

790.3 ± 1.6 782.5 ± 2.1 774.7 ± 2.5 MW = 158.28

220

Table 1. Experimental and recommended values with uncertainties. T K 293.15 293.15 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

826.2 ± 2.0 823.8 ± 2.0 825.0 ± 2.2

57-pet/nef-1 59-asi/gei Recommended

Landolt-Börnstein New Series IV/8G

2.1.6 Alkanols, C10 5-Decanol

[5205-34-5]

179 C10H22O

MW = 158.28

221

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.221. Coefficient ρ = A + BT 1047.15 A B −0.760 Table 2. Experimental values with uncertainties and deviation from calculated values. T K 293.15 293.15 298.15 1)

ρexp ± 2σ est −3

kg ⋅ m

827.6 ± 3.0 823.8 ± 1.0 820.6 ± 0.4

ρexp − ρcalc

Ref.

kg ⋅ m−3

56-gol/kon1) 59-asi/gei 88-cac/cos

3.29 −0.55 0.09

Not included in calculation of linear coefficients.

Table 3. Recommended values. ρexp ± 2σ est

T K

kg ⋅ m−3

826.7 ± 0.6 824.4 ± 0.5 820.6 ± 0.5

290.00 293.15 298.15

2,2-Dimethyl-4-ethyl-3-hexanol

[66719-47-9]

C10H22O

MW = 158.28

222

C10H22O

MW = 158.28

223

C10H22O

MW = 158.28

224

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

−3

kg ⋅ m

833.9 ± 1.0

41-whi/whi

2,4-Dimethyl-4-ethyl-3-hexanol

[66719-48-0]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

860.6 ± 2.0

53-sok

5,5-Dimethyl-2-ethyl-1-hexanol

[66719-49-1]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

kg ⋅ m−3

838.6 ± 1.0

Landolt-Börnstein New Series IV/8G

56-gol/kon

180

2.1.6 Alkanols, C10

5,5-Dimethyl-3-ethyl-3-hexanol

[5340-62-5]

C10H22O

MW = 158.28

225

C10H22O

MW = 158.28

226

C10H22O

MW = 158.28

227

Table 1. Experimental and recommended values with uncertainties. T K

293.15 293.15 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

842.2 ± 1.0 845.0 ± 2.0 842.8 ± 1.4

34-sta 42-whi/for Recommended

2,4-Dimethyl-3-(1-methylethyl)3-pentanol

[51200-83-0]

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.050. Coefficient ρ = A + BT 1097.67 A B −0.800

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 293.15 292.15 293.15 298.15 1)

ρexp ± 2σ est −3

kg ⋅ m

874.0 ± 2.0 861.6 ± 2.0 863.2 ± 0.6 859.1 ± 0.6

ρexp − ρcalc

Ref.

kg ⋅ m−3

44-you/rob1) 46-vav/col1) 47-how/mea 47-how/mea

10.85 −2.35 0.05 −0.05

Not included in calculation of linear coefficients.

Table 3. Recommended values. T K 290.00 293.15 298.15

ρexp ± 2σ est kg ⋅ m−3

865.7 ± 0.4 863.1 ± 0.3 859.1 ± 0.3

2,4-Dimethyl-3-propyl-3-pentanol

[500001-19-4]

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 0.262. Coefficient ρ = A + BT 1088.19 A B −0.800 cont. Landolt-Börnstein New Series IV/8G

2.1.6 Alkanols, C10

181

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 293.15 273.15 303.15

ρexp ± 2σ est

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−3

kg ⋅ m

853.9 ± 1.0 869.3 ± 1.0 845.8 ± 1.0

0.23 −0.37 0.13

26-sta 26-sta 26-sta

Table 3. Recommended values. ρexp ± 2σ est

T K 270.00 280.00

ρexp ± 2σ est

T K 290.00 293.15

−3

kg ⋅ m

872.2 ± 2.2 864.2 ± 1.4

1,1-Dimethyl-1-octanol

−3

kg ⋅ m

856.2 ± 0.9 853.7 ± 1.0 [10297-57-1]

T K 298.15 310.00

ρexp ± 2σ est kg ⋅ m−3

849.7 ± 1.3 840.2 ± 2.2

C10H22O

MW = 158.28

228

C10H22O

MW = 158.28

229

C10H22O

MW = 158.28

230

C10H22O

MW = 158.28

231

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

807.8 ± 1.0

64-tis/sta

2,2-Dimethyl-1-octanol

[2370-14-1]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est

T K

293.15 293.15 293.15 1)

Ref.

−3

kg ⋅ m

830.0 ± 1.0 843.0 ± 2.0 830.0 ± 1.0

64-blo/hag 65-shu/puz1) Recommended

Not included in calculation of recommended value.

2,2-Dimethyl-4-octanol

[66719-52-6]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

−3

kg ⋅ m

821.2 ± 1.0

2,3-Dimethyl-3-octanol

38-whi/pop-1 [19781-10-3]

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.150. Coefficient ρ = A + BT 1069.53 A B −0.820 cont.

Landolt-Börnstein New Series IV/8G

182

2.1.6 Alkanols, C10

2,3-Dimethyl-3-octanol (cont.) Table 2. Experimental values with uncertainties and deviation from calculated values. T K

293.15 293.15 298.15 1)

ρexp ± 2σ est −3

kg ⋅ m

840.1 ± 6.0 829.3 ± 0.6 824.9 ± 0.6

ρexp − ρcalc

Ref.

−3

kg ⋅ m

33-whi/eve1) 50-mea/foo 50-mea/foo

10.95 0.15 −0.15

Not included in calculation of linear coefficients.

Table 3. Recommended values. T K

290.00 293.15 298.15

ρexp ± 2σ est kg ⋅ m−3

831.7 ± 0.7 829.2 ± 0.5 825.1 ± 0.5

2,4-Dimethyl-2-octanol

[18675-20-2]

C10H22O

MW = 158.28

232

C10H22O

MW = 158.28

233

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

825.7 ± 2.0

48-naz/tor

2,4-Dimethyl-4-octanol

[33933-79-8]

Table 1. Experimental and recommended values with uncertainties. T K

293.15 293.15 293.15 1)

ρexp ± 2σ est

T K

Ref.

−3

kg ⋅ m

823.8 ± 1.0 823.6 ± 1.0 832.8 ± 6.0

33-mey/tuo 58-sok/kra 59-nog/dza1)

293.15 293.15 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

822.7 ± 1.0 822.7 ± 1.0 823.2 ± 1.0

59-pet/zak 59-pet/zak-1 Recommended

Not included in calculation of recommended value.

2,5-Dimethyl-4-octanol

[66719-53-7]

C10H22O

MW = 158.28

234

C10H22O

MW = 158.28

235

Table 1. Experimental value with uncertainty. T K

298.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

821.5 ± 0.8

12-bje

2,6-Dimethyl-1-octanol

[62417-08-7]

Table 1. Experimental value with uncertainty. T K 291.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

830.0 ± 2.0

14-vav Landolt-Börnstein New Series IV/8G

2.1.6 Alkanols, C10

2,6-Dimethyl-2-octanol

[18479-57-7]

183

C10H22O

MW = 158.28

236

C10H22O

MW = 158.28

237

C 10H22O

MW = 158.28

238

Table 1. Experimental and recommended values with uncertainties. T K 298.15 293.15 293.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

802.3 ± 10.0 833.5 ± 5.0 826.0 ± 2.0 827.3 ± 1.0 827.3 ± 1.0

53-sut1) 57-naz/kra1) 59-hou/lev1) 64-ohl/sei Recommended

Not included in calculation of recommended value.

2,7-Dimethyl-1-octanol

[15250-22-3]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

288.15

Ref.

kg ⋅ m−3

830.3 ± 1.0

40-pal

2,7-Dimethyl-2-octanol

[42007-73-8]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 7.1829 · 10−2 (combined temperature ranges, weighted), σc,uw = 1.9108 · 10−2 (combined temperature ranges, unweighted). Coefficient A B

T = 293.15 to 358.15 K ρ = A + BT + CT 2 + DT 3 + … 1.06429 · 103 −8.15665 · 10−1

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 293.15 298.15 303.15 313.15 323.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

825.10 ± 1.00 821.10 ± 1.00 817.00 ± 1.00 808.90 ± 1.00 800.70 ± 1.00

−0.08 0.00 −0.02 0.04 −0.01

Ref. (Symbol in Fig. 1)

) ) ) ) )

55-kus( 55-kus( 55-kus( 55-kus( 55-kus(

T K 333.15 343.15 353.15 358.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

792.60 ± 1.00 784.50 ± 1.00 776.20 ± 1.00 772.10 ± 1.00

0.05 0.11 −0.04 −0.06

Ref. (Symbol in Fig. 1)

) ) ) )

55-kus( 55-kus( 55-kus( 55-kus(

cont.

Landolt-Börnstein New Series IV/8G

184

2.1.6 Alkanols, C10

ρ

ρ

2,7-Dimethyl-2-octanol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

290.00 293.15 298.15 300.00

ρ ± σ fit kg ⋅ m−3

ρ ± σ fit kg ⋅ m−3

T K

827.75 ± 1.27 825.18 ± 1.23 821.10 ± 1.16 819.59 ± 1.13

811.43 ± 0.98 803.28 ± 0.86 795.12 ± 0.81 786.96 ± 0.88

310.00 320.00 330.00 340.00

2,7-Dimethyl-3-octanol

[66719-55-9]

T K

350.00 360.00 370.00

C10H22O

ρ ± σ fit kg ⋅ m−3 778.81 ± 1.09 770.65 ± 1.48 762.49 ± 2.10

MW = 158.28

239

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

815.2 ± 2.0

12-mic

Landolt-Börnstein New Series IV/8G

2.1.6 Alkanols, C10 2,7-Dimethyl-4-octanol

[19781-11-4]

185 C10H22O

MW = 158.28

240

C10H22O

MW = 158.28

241

C10H22O

MW = 158.28

242

C10H22O

MW = 158.28

243

Table 1. Experimental and recommended values with uncertainties. T K 293.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

814.0 ± 2.0 818.3 ± 1.0 818.3 ± 1.0

36-tuo1) 44-pow/hag Recommended

Not included in calculation of recommended value.

3,5-Dimethyl-3-octanol

[56065-42-0]

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

837.0 ± 2.0

59-col/gau

3,6-Dimethyl-3-octanol

[151-19-9]

Table 1. Experimental value with uncertainty. T K 295.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

834.7 ± 2.0

13-dup

3,7-Dimethyl-1-octanol

[106-21-8]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est

T K

291.15 293.15 284.15 288.15 293.15 291.15 1)

T K

Ref.

kg ⋅ m−3

838.0 ± 2.0 831.0 ± 3.0 837.4 ± 3.0 830.0 ± 6.0 835.7 ± 3.0 837.0 ± 3.0

23-von/kai1) 24-lon/mar1) 28-esc1) 40-pal1) 51-sor/suc1) 52-ino1)

296.15 293.15 293.15 294.15 293.15 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

828.1 ± 3.0 840.2 ± 1.5 828.6 ± 3.0 840.0 ± 2.0 840.9 ± 1.5 840.6 ± 1.5

54-rin/ari1) 58-leb/kuk 60-por/far1) 61-yeh1) 63-yeh Recommended

Not included in calculation of recommended value.

3,7-Dimethyl-2-octanol

[15340-96-2]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

829.1 ± 1.0

Landolt-Börnstein New Series IV/8G

56-nav/des

C10H22O

MW = 158.28

244

186

2.1.6 Alkanols, C10

3,7-Dimethyl-3-octanol

[78-69-3]

C10H22O

MW = 158.28

245

C10H22O

MW = 158.28

246

C10H22O

MW = 158.28

247

C10H22O

MW = 158.28

248

C10H22O

MW = 158.28

249

Table 1. Experimental and recommended values with uncertainties. T K 293.15 298.15 292.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

kg ⋅ m−3

828.0 ± 2.0 864.7 ± 20.0 833.9 ± 3.0 829.5 ± 2.0 828.7 ± 2.1

14-wal-1 39-ste/mcn1) 40-pal1) 58-naz/gus Recommended

Not included in calculation of recommended value.

4,6-Dimethyl-4-octanol

[56065-43-1]

Table 1. Experimental value with uncertainty. T K 301.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

825.8 ± 1.0

60-tha/vas

4,7-Dimethyl-4-octanol

[19781-13-6]

Table 1. Experimental value with uncertainty. T K 273.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

842.1 ± 2.0

12-gue-1

3-Ethyl-2-methyl-3-heptanol

[66719-37-7]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

845.5 ± 2.0

15-wal-3

3-Ethyl-6-methyl-3-heptanol

[66719-40-2]

Table 1. Fit with estimated B coefficient for 4 accepted points. Deviation σw = 0.056. Coefficient ρ = A + BT 1065.11 A B −0.780 Table 2. Experimental values with uncertainties and deviation from calculated values. T K 273.15 283.55 273.15 283.55

ρexp ± 2σ est −3

kg ⋅ m

852.0 ± 1.5 844.0 ± 1.5 852.0 ± 1.5 844.0 ± 1.5

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−0.06 0.06 −0.06 0.06

04-gri 04-gri 04-gri-1 04-gri-1 cont. Landolt-Börnstein New Series IV/8G

2.1.6 Alkanols, C10

187

Table 3. Recommended values. ρexp ± 2σ est

T K

kg ⋅ m−3

854.5 ± 1.5 846.7 ± 1.3 838.9 ± 1.6

270.00 280.00 290.00

5-Ethyl-4-methyl-3-heptanol

[66731-94-0]

C10H22O

MW = 158.28

250

C10H22O

MW = 158.28

251

C10H22O

MW = 158.28

252

C10H22O

MW = 158.28

253

Table 1. Experimental value with uncertainty. T K 290.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

865.0 ± 2.0

43-col/jol

l-3-Ethyl-1-octanol

[900002-57-5]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

295.15

Ref.

−3

kg ⋅ m

833.0 ± 2.0

31-lev/mar-3

3-Ethyl-3-octanol

[2051-32-3]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

298.15

Ref.

−3

kg ⋅ m

836.1 ± 1.0

33-whi/wil

4-Ethyl-4-octanol

[38395-42-5]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 2.1329 · 10−1 (combined temperature ranges, weighted), σc,uw = 9.5387 · 10−2 (combined temperature ranges, unweighted). T = 273.15 to 338.15 K ρ = A + BT + CT 2 + DT 3 + … 1.07866 · 103 −8.43628 · 10−1

Coefficient A B

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 273.15 298.15 308.15

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

848.50 ± 1.00 826.80 ± 1.00 818.50 ± 1.00

0.28 −0.33 −0.19

kg ⋅ m

T K 39-owe/qua(✕ ) 318.15 39-owe/qua(✕ ) 328.15 39-owe/qua(✕ ) 338.15

Ref. (Symbol in Fig. 1)

ρexp ± 2σ est −3

kg ⋅ m

810.20 ± 1.00 802.00 ± 1.00 793.50 ± 1.00

ρexp − ρcalc kg ⋅ m−3

−0.06 0.18 0.12

Ref. (Symbol in Fig. 1) 39-owe/qua(✕ ) 39-owe/qua(✕ ) 39-owe/qua(✕ ) cont.

Landolt-Börnstein New Series IV/8G

188

2.1.6 Alkanols, C10

4-Ethyl-4-octanol (cont.)

ρ

ρ

Further references: [33-whi/woo].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc - T )4] ). T K

270.00 280.00 290.00 293.15

ρ ± σ fit kg ⋅ m−3

ρ ± σ fit kg ⋅ m−3

T K

850.88 ± 1.27 842.44 ± 1.16 834.00 ± 1.08 831.35 ± 1.06

827.13 ± 1.03 825.57 ± 1.02 817.13 ± 1.00 808.70 ± 1.02

298.15 300.00 310.00 320.00

6-Ethyl-3-octanol

[19781-27-2]

T K

330.00 340.00 350.00

C10H22O

ρ ± σ fit kg ⋅ m−3 800.26 ± 1.07 791.82 ± 1.15 783.39 ± 1.26

MW = 158.28

254

Table 1. Experimental value with uncertainty. T K 297.65

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

839.6 ± 0.5

36-pow/bal

Landolt-Börnstein New Series IV/8G

2.1.6 Alkanols, C10 3-Ethyl-2,2,4-trimethyl-3-pentanol

[66256-41-5]

189 C10H22O

MW = 158.28

255

MW = 158.28

256

MW = 158.28

257

C10H22O

MW = 158.28

258

C10H22O

MW = 158.28

259

Table 1. Experimental and recommended values with uncertainties. T K 292.15 293.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

862.8 ± 1.5 862.0 ± 1.0 862.8 ± 1.0 862.4 ± 1.0

36-naz1) 51-smi/cre 54-mos/cox Recommended

Not included in calculation of recommended value.

2-Methyl-3-(1-methylethyl)-3-hexanol

[51200-81-8]

C10H22O

Table 1. Experimental and recommended values with uncertainties. T K 293.15 293.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

853.7 ± 2.0 855.4 ± 3.0 850.4 ± 1.0 851.1 ± 1.2

26-sta 43-geo1) 48-cad/foo Recommended

Not included in calculation of recommended value.

5-Methyl-2-(1-methylethyl)-1-hexanol

[2051-33-4]

C10H22O

Table 1. Experimental and recommended values with uncertainties. T K 293.15 290.15 290.15 1)

ρexp ± 2σ est

Ref.

kg ⋅ m−3

832.2 ± 2.0 836.6 ± 1.0 836.6 ± 1.0

25-ter1) 47-sch/sch Recommended

Not included in calculation of recommended value.

4-Methyl-2-(2-methylpropyl)-1-pentanol [22417-45-4] Table 1. Experimental values with uncertainties. T K 277.15 273.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

846.0 ± 2.0 846.0 ± 2.0

2-Methyl-1-nonanol

04-bou/bla 10-fre [40589-14-8]

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.350. Coefficient ρ = A + BT 1058.41 A B −0.780 cont. Landolt-Börnstein New Series IV/8G

190

2.1.6 Alkanols, C10

2-Methyl-1-nonanol (cont.) Table 2. Experimental values with uncertainties and deviation from calculated values. T K

273.15 288.15

ρexp ± 2σ est −3

kg ⋅ m

845.7 ± 2.0 833.3 ± 2.0

ρexp − ρcalc

Ref.

−3

kg ⋅ m

0.35 −0.35

02-gue 02-gue

Table 3. Recommended values. T K 270.00 280.00 290.00

ρexp ± 2σ est kg ⋅ m−3

847.8 ± 2.1 840.0 ± 1.8 832.2 ± 2.0

2-Methyl-3-nonanol

[26533-33-5]

C10H22O

MW = 158.28

260

C10H22O

MW = 158.28

261

Table 1. Fit with estimated B coefficient for 4 accepted points. Deviation σw = 0.309. Coefficient ρ = A + BT 1051.17 A B −0.760 Table 2. Experimental values with uncertainties and deviation from calculated values. T K 293.15 293.15 293.15 298.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

829.0 ± 1.0 828.7 ± 1.0 828.1 ± 0.6 824.5 ± 0.6

Ref.

0.63 0.33 −0.27 −0.07

12-pic/ken 48-pet/old 50-mea/foo 50-mea/foo

Table 3. Recommended values. T K 290.00 293.15 298.15

ρexp ± 2σ est kg ⋅ m−3

830.8 ± 0.8 828.4 ± 0.8 824.6 ± 0.8

2-Methyl-4-nonanol

[26533-31-3]

Table 1. Experimental value with uncertainty. T K

298.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

820.0 ± 2.0

54-dub/luf

Landolt-Börnstein New Series IV/8G

2.1.6 Alkanols, C10 2-Methyl-5-nonanol

[29843-62-7]

191 C10H22O

MW = 158.28

262

C10H22O

MW = 158.28

263

C10H22O

MW = 158.28

264

C10H22O

MW = 158.28

265

C10H22O

MW = 158.28

266

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

821.5 ± 1.0

44-pow/hag

3-Methyl-1-nonanol

[22663-64-5]

Table 1. Experimental and recommended values with uncertainties. T K 293.15 296.15 296.15 1)

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

834.2 ± 3.0 837.0 ± 2.0 837.0 ± 2.0

22-lev/tay-11) 31-lev/mar-5 Recommended

Not included in calculation of recommended value.

(R)-3-Methyl-1-nonanol

[86414-45-1]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

829.0 ± 2.0

58-leg/ulr

3-Methyl-2-nonanol

[60671-32-1]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est

T K

295.15 293.15 293.15 1)

Ref.

kg ⋅ m−3

845.0 ± 3.0 835.3 ± 2.0 835.3 ± 2.0

35-gre-21) 57-pet/nef-1 Recommended

Not included in calculation of recommended value.

3-Methyl-3-nonanol

[21078-72-8]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 1.0876 (combined temperature ranges, weighted), σc,uw = 6.1414 · 10−1 (combined temperature ranges, unweighted). Coefficient A B

T = 273.15 to 338.15 K ρ = A + BT + CT 2 + DT 3 + … 1.07303 · 103 −8.27037 · 10−1 cont.

Landolt-Börnstein New Series IV/8G

192

2.1.6 Alkanols, C10

3-Methyl-3-nonanol (cont.) Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

kg ⋅ m

Ref. (Symbol in Fig. 1)

829.00 ± 3.00 831.10 ± 1.00 845.50 ± 1.00 825.10 ± 1.00 817.30 ± 1.00

0.90 0.52 −1.62 −1.34 −0.87

35-gre-2(∇) 38-whi/ore( 39-owe/qua( 39-owe/qua( 39-owe/qua(

kg ⋅ m

−3

) ) ) )

T K

318.15 328.15 338.15 293.15

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

809.20 ± 1.00 801.00 ± 1.00 792.70 ± 1.00 835.00 ± 3.00

−0.70 −0.63 −0.66 4.42

kg ⋅ m

Ref. (Symbol in Fig. 1)

39-owe/qua( ) 39-owe/qua( ) 39-owe/qua( ) 61-sok/she(∆)

ρ

ρ

296.15 293.15 273.15 298.15 308.15

ρexp − ρcalc

−3

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15

ρ ± σ fit kg ⋅ m−3 849.73 ± 2.09 841.46 ± 2.08 833.19 ± 2.05 830.58 ± 2.01

T K

298.15 300.00 310.00 320.00

ρ ± σ fit kg ⋅ m−3 826.44 ± 1.86 824.91 ± 1.79 816.64 ± 1.29 808.37 ± 0.89

T K

330.00 340.00 350.00

ρ ± σ fit kg ⋅ m−3 800.10 ± 0.87 791.83 ± 1.44 783.56 ± 2.91

Landolt-Börnstein New Series IV/8G

2.1.6 Alkanols, C10 d-3-Methyl-5-nonanol

[500021-26-1]

193 C10H22O

MW = 158.28

267

C10H22O

MW = 158.28

268

C10H22O

MW = 158.28

269

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

821.0 ± 2.0

50-let/tra

4-Methyl-1-nonanol

[1489-47-0]

Table 1. Experimental value with uncertainty. T K 300.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

826.0 ± 2.0

31-lev/mar-5

4-Methyl-4-nonanol

[23418-38-4]

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 0.047. Coefficient ρ = A + BT 1071.65 A B −0.820 Table 2. Experimental values with uncertainties and deviation from calculated values. T K 298.15 298.15 318.15 328.15 1)

ρexp ± 2σ est

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−3

kg ⋅ m

824.5 ± 2.0 827.1 ± 1.0 810.8 ± 1.0 802.6 ± 1.0

−2.67 −0.07 0.03 0.03

33-whi/wil1) 44-qua/sma 44-qua/sma 44-qua/sma

Not included in calculation of linear coefficients.

Table 3. Recommended values. ρexp ± 2σ est

T K

kg ⋅ m

833.8 ± 1.4 831.3 ± 1.3

290.00 293.15

ρexp ± 2σ est

T K

−3

−3

kg ⋅ m

827.2 ± 1.1 817.4 ± 0.7

298.15 310.00

5-Methyl-1-nonanol

[2768-16-3]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

297.15

Ref.

kg ⋅ m−3

831.0 ± 2.0

Landolt-Börnstein New Series IV/8G

33-lev/mar-1

T K

320.00 330.00

C10H22O

ρexp ± 2σ est kg ⋅ m−3

809.2 ± 0.7 801.0 ± 1.0

MW = 158.28

270

194

2.1.6 Alkanols, C10

5-Methyl-4-nonanol

[66719-44-6]

C10H22O

MW = 158.28

271

C10H22O

MW = 158.28

272

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 300.15 48-pow/nie 826.0 ± 2.0 5-Methyl-5-nonanol

[33933-78-7]

Table 1. Fit with estimated B coefficient for 5 accepted points. Deviation σw = 0.264. Coefficient ρ = A + BT 1063.90 A B −0.800 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. ρexp − ρcalc Ref. ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 293.15 829.0 ± 1.0 33-whi/woo 328.15 801.3 ± 1.0 44-qua/sma −0.38 −0.08 298.15 825.3 ± 1.0 33-whi/woo 318.15 0.12 44-qua/sma 809.5 ± 1.0 −0.08 298.15 825.8 ± 1.0 0.42 44-qua/sma 293.15 830.5 ± 2.0 1.12 59-yur/bel1) 1)

Not included in calculation of recommended value.

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 290.00 831.9 ± 1.2 293.15 829.4 ± 1.1 6-Methyl-2-nonanol

ρexp ± 2σ est

T K 298.15 310.00

kg ⋅ m−3

825.4 ± 0.9 815.9 ± 0.8 [66256-60-8]

T K 320.00 330.00

ρexp ± 2σ est kg ⋅ m−3

807.9 ± 1.0 799.9 ± 1.4

C10H22O

MW = 158.28

273

C10H22O

MW = 158.28

274

C10H22O

MW = 158.28

275

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 61-shv/pet 833.2 ± 1.0 7-Methyl-1-nonanol

[33234-93-4]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 62-lar/sal 828.2 ± 1.0 L(+)-7-Methyl-1-nonanol

[500006-91-7]

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

828.2 ± 0.6

62-lar/sal Landolt-Börnstein New Series IV/8G

2.1.6 Alkanols, C10 3-(1-Methylethyl)-1-heptanol

[38514-15-7]

195

C10H22O

MW = 158.28

276

C10H22O

MW = 158.28

277

Table 1. Experimental value with uncertainty. T K

303.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

834.1 ± 1.0

57-kit

4-(1-Methylethyl)-4-heptanol

[51200-82-9]

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 0.713. Coefficient ρ = A + BT 1067.93 A B −0.760 Table 2. Experimental values with uncertainties and deviation from calculated values. T K

293.15 273.15 303.15 293.15 1)

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

844.9 ± 2.0 859.6 ± 2.0 838.5 ± 2.0 847.1 ± 3.0

Ref.

−0.23 −0.73 0.97 1.97

26-sta 26-sta 26-sta 54-naz/kak-31)

Not included in calculation of recommended value.

Table 3. Recommended values. ρexp ± 2σ est

T K

862.7 ± 2.5 855.1 ± 1.8

270.00 280.00

ρexp ± 2σ est

T K

kg ⋅ m−3

kg ⋅ m−3

847.5 ± 1.5 845.1 ± 1.6

290.00 293.15

2-(1-Methylpropyl)-3-methyl-1-pentanol [91717-78-1]

T K

298.15 310.00

ρexp ± 2σ est kg ⋅ m−3

841.3 ± 1.7 832.3 ± 2.5

C10H22O

MW = 158.28

278

C10H22O

MW = 158.28

279

Table 1. Experimental value with uncertainty. T K 295.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

835.0 ± 2.0

62-thi

2-Propyl-1-heptanol

[10042-59-8]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

−3

kg ⋅ m

832.2 ± 0.4

Landolt-Börnstein New Series IV/8G

56-ano-4

196

2.1.6 Alkanols, C10

4-Propyl-4-heptanol

[2198-72-3]

C10H22O

MW = 158.28

280

C10H22O

MW = 158.28

281

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 0.630. Coefficient ρ = A + BT 1067.17 A B −0.800 Table 2. Experimental values with uncertainties and deviation from calculated values. T K

294.15 290.35 293.15 298.15 1)

ρexp ± 2σ est −3

kg ⋅ m

833.7 ± 2.0 835.0 ± 1.0 834.0 ± 1.0 828.3 ± 0.5

ρexp − ρcalc

Ref.

kg ⋅ m−3

02-kon1) 19-eyk 61-mes/erz 88-cac/cos

1.85 0.11 1.35 −0.37

Not included in calculation of linear coefficients.

Table 3. Recommended values. T K

290.00 293.15 298.15

ρexp ± 2σ est kg ⋅ m−3

835.2 ± 1.0 832.6 ± 0.9 828.6 ± 0.9

2,2,3,4-Tetramethyl-3-hexanol

[66256-63-1]

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.080. Coefficient ρ = A + BT 1104.69 A B −0.840 Table 2. Experimental values with uncertainties and deviation from calculated values. T K

283.15 293.15

ρexp ± 2σ est −3

kg ⋅ m

867.0 ± 2.0 858.4 ± 1.0

ρexp − ρcalc

Ref.

−3

kg ⋅ m

0.16 −0.04

37-naz 50-ste/coo

Table 3. Recommended values. T K 280.00 290.00 293.15 298.15

ρexp ± 2σ est kg ⋅ m−3

869.5 ± 1.7 861.1 ± 1.3 858.4 ± 1.4 854.2 ± 1.5

Landolt-Börnstein New Series IV/8G

2.1.6 Alkanols, C10 2,2,3,5-Tetramethyl-3-hexanol

[66256-64-2]

197 C10H22O

MW = 158.28

282

C10H22O

MW = 158.28

283

C10H22O

MW = 158.28

284

C10H22O

MW = 158.28

285

C10H22O

MW = 158.28

286

C10H22O

MW = 158.28

287

Table 1. Experimental values with uncertainties. T K 293.15 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

839.3 ± 1.0 839.3 ± 1.0

55-pet 55-pet/sus

2,2,4,4-Tetramethyl-3-hexanol

[66256-65-3]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

854.9 ± 1.0

34-sta

2,3,4,4-Tetramethyl-3-hexanol

[66256-67-5]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est

T K

289.15 293.15 293.15 293.15 1)

Ref.

kg ⋅ m−3

876.0 ± 2.0 869.4 ± 3.0 874.5 ± 1.0 874.5 ± 1.0

37-naz1) 40-mos1) 50-ste/coo Recommended

Not included in calculation of recommended value.

2,3,5,5-Tetramethyl-3-hexanol

[5396-09-8]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

kg ⋅ m−3

837.8 ± 2.0

42-moe

3,4,4,5-Tetramethyl-3-hexanol

[66256-39-1]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

kg ⋅ m−3

874.2 ± 1.0

50-ste/coo

3,4,5,5-Tetramethyl-3-hexanol

[66256-40-4]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

862.3 ± 1.0

Landolt-Börnstein New Series IV/8G

50-ste/coo

198

2.1.6 Alkanols, C10

2,2,3-Trimethyl-3-heptanol

[29772-40-5]

C10H22O

MW = 158.28

288

C10H22O

MW = 158.28

289

C10H22O

MW = 158.28

290

C10H22O

MW = 158.28

291

C10H22O

MW = 158.28

292

C10H22O

MW = 158.28

293

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

848.7 ± 1.0

29-con/bla

2,2,4-Trimethyl-4-heptanol

[57233-31-5]

Table 1. Experimental values with uncertainties. T K

293.15 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

833.0 ± 2.0 833.0 ± 2.0

42-moe 49-moe/whi

2,2,5-Trimethyl-4-heptanol

[66256-42-6]

Table 1. Experimental value with uncertainty. T K

289.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

751.3 ± 1.0

39-pet/sum

2,2,6-Trimethyl-3-heptanol

[66256-43-7]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

823.6 ± 1.0

38-whi/mey

2,3,6-Trimethyl-3-heptanol

[58046-40-5]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

839.8 ± 1.0

63-tho/pal

2,4,6-Trimethyl-4-heptanol

[60836-07-9]

Table 1. Experimental and recommended values with uncertainties. T K 294.15 293.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

823.0 ± 2.0 818.6 ± 3.0 824.1 ± 1.0 824.1 ± 1.0

09-bod/tab1) 33-mey/tuo1) 59-pet/zak-1 Recommended

Not included in calculation of recommended value.

Landolt-Börnstein New Series IV/8G

2.1.6 Alkanols, C10 2,5,5-Trimethyl-4-heptanol

[66256-49-3]

199 C10H22O

MW = 158.28

294

C10H22O

MW = 158.28

295

C10H22O

MW = 158.28

296

C10H22O

MW = 158.28

297

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

838.0 ± 2.0

57-tak/nak

2,5,6-Trimethyl-2-heptanol

[66256-48-2]

Table 1. Experimental value with uncertainty. T K 291.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

833.0 ± 2.0

11-wal

3,5,5-Trimethyl-3-heptanol

[66256-50-6]

Table 1. Experimental and recommended values with uncertainties. T K 293.15 293.15 293.15 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

851.3 ± 2.0 851.3 ± 2.0 855.8 ± 1.0 854.3 ± 1.6

40-mos 41-whi/mos 50-ste/coo Recommended

4,6,6-Trimethyl-2-heptanol

[51079-79-9]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

kg ⋅ m−3

826.5 ± 2.0

Landolt-Börnstein New Series IV/8G

46-dou-1

2.1.7 Alkanols, C11 - C12

201

2.1.7 Alkanols, C11 - C12 3-Butyl-2,4-dimethyl-3-pentanol

[900002-65-5]

C11H24O

MW = 172.31

298

C11H24O

MW = 172.31

299

C11H24O

MW = 172.31

300

C11H24O

MW = 172.31

301

C11H24O

MW = 172.31

302

C11H24O

MW = 172.31

303

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 44-you/rob 860.0 ± 2.0 3-Butyl-2-heptanol

[115667-95-3]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 291.05 25-hes/bap 839.2 ± 1.0 2,6-Dimethyl-4-ethyl-4-heptanol

[54460-99-0]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 298.15 56-kru/cho 825.2 ± 0.8 3,3-Dimethyl-5-ethyl-4-heptanol

[500000-48-6]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 41-whi/whi 849.6 ± 1.0 l-2,4-Dimethyl-3-(1-methylethyl)3-hexanol

[28357-71-3]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 44-you/rob 868.0 ± 2.0 2,5-Dimethyl-3-(1-methylethyl)3-hexanol

[57233-26-8]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 43-geo 847.0 ± 2.0 293.15 48-cad/foo 848.6 ± 1.0 293.15 Recommended 848.3 ± 1.0

Landolt-Börnstein New Series IV/8G

202

2.1.7 Alkanols, C11 - C12

2,2-Dimethyl-1-nonanol

[14250-80-7]

C11H24O

MW = 172.31

304

C11H24O

MW = 172.31

305

C11H24O

MW = 172.31

306

C11H24O

MW = 172.31

307

C11H24O

MW = 172.31

308

C11H24O

MW = 172.31

309

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

839.2 ± 1.0

65-shu/puz

2,2-Dimethyl-4-nonanol

[38206-58-5]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

822.5 ± 1.0

38-whi/pop-1

2,4-Dimethyl-4-nonanol

[74356-31-3]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

828.5 ± 2.0

59-pet/zak

2,6-Dimethyl-5-nonanol

[500001-10-5]

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

821.6 ± 0.8

12-bje

3,5-Dimethyl-5-nonanol

[106593-61-7]

Table 1. Experimental value with uncertainty. T K 301.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

826.4 ± 1.0

60-tha/vas

4,8-Dimethyl-1-nonanol

[33933-80-1]

Table 1. Experimental values with uncertainties. T K 292.15 291.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

834.0 ± 2.0 833.0 ± 2.0

23-von/kai 23-von/kai

Landolt-Börnstein New Series IV/8G

2.1.7 Alkanols, C11 - C12 4,8-Dimethyl-4-nonanol

[91337-13-2]

203

C11H24O

MW = 172.31

310

C11H24O

MW = 172.31

311

C11H24O

MW = 172.31

312

C11H24O

MW = 172.31

313

Table 1. Experimental value with uncertainty. T K 284.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

845.8 ± 2.0

28-esc

2,2-Dimethyl-3-propyl-3-hexanol

[900002-63-3]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

291.15

Ref.

kg ⋅ m−3

853.0 ± 2.0

21-ler

4,4-Dimethyl-3-(1,1-dimethylethyl)1-pentanol

[79802-55-4]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

866.1 ± 2.0

60-pet/sok

5-Ethyl-2-nonanol

[103-08-2]

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.150. Coefficient ρ = A + BT 1063.31 A B −0.780 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

303.15 293.15

−3

kg ⋅ m

826.7 ± 1.0 834.8 ± 1.0

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−0.15 0.15

48-wei 58-ano-13

Table 3. Recommended values. T K 290.00 293.15

ρexp ± 2σ est kg ⋅ m−3

837.1 ± 1.0 834.7 ± 0.9

T K 298.15 310.00

5-Ethyl-3-nonanol

ρexp ± 2σ est kg ⋅ m−3

830.7 ± 0.9 821.5 ± 1.1 [19780-71-3]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

834.9 ± 1.0

Landolt-Börnstein New Series IV/8G

58-ano-5

C11H24O

MW = 172.31

314

204

2.1.7 Alkanols, C11 - C12

5-Ethyl-4-nonanol

[19780-73-5]

C11H24O

MW = 172.31

315

C11H24O

MW = 172.31

316

Table 1. Experimental value with uncertainty. T K 289.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

837.0 ± 2.0

48-pow/nie

5-Ethyl-5-nonanol

[5340-51-2]

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.150. Coefficient ρ = A + BT 1037.09 A B −0.680 Table 2. Experimental values with uncertainties and deviation from calculated values. T K 293.15 298.15

ρexp ± 2σ est −3

kg ⋅ m

837.6 ± 1.0 834.5 ± 1.0

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−0.15 0.15

33-whi/woo 33-whi/woo

Table 3. Recommended values. T K 290.00 293.15 298.15

ρexp ± 2σ est kg ⋅ m−3

839.9 ± 1.1 837.8 ± 0.9 834.4 ± 0.9

d-6-Ethyl-3-nonanol

[900002-60-0]

C11H24O

MW = 172.31

317

C11H24O

MW = 172.31

318

C11H24O

MW = 172.31

319

Table 1. Experimental value with uncertainty. T K 295.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

830.0 ± 2.0

31-lev/mar-3

3-Ethyl-2,2,4,4-tetramethyl-3-pentanol

[32579-68-3]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

811.9 ± 1.5

60-pet/sok

4-Ethyl-2,2,3-trimethyl-3-hexanol

[91337-10-9]

Table 1. Experimental value with uncertainty. T K 289.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

862.0 ± 2.0

37-naz

Landolt-Börnstein New Series IV/8G

2.1.7 Alkanols, C11 - C12 2-Methyl-4-decanol

[25564-57-2]

205

C11H24O

MW = 172.31

320

C11H24O

MW = 172.31

321

C11H24O

MW = 172.31

322

C11H24O

MW = 172.31

323

C11H24O

MW = 172.31

324

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 38-wer/bog 816.8 ± 1.0 2-Methyl-5-decanol

[500001-13-8]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 44-pow/hag 826.6 ± 1.0 3-Methyl-2-decanol

[500001-16-1]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 296.15 33-pow/mur 834.0 ± 2.0 4-Methyl-3-decanol

[500001-14-9]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 296.15 35-gre-2 829.0 ± 2.0 4-Methyl-4-decanol

[26209-94-9]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 4.1396 · 10−1 (combined temperature ranges, weighted), σc,uw = 2.6273 · 10−1 (combined temperature ranges, unweighted). Coefficient A B

T = 273.15 to 338.15 K ρ = A + BT + CT 2 + DT 3 + … 1.06090 · 103 −7.94286 · 10−1

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 293.15 829.60 ± 1.00 1.54 38-whi/ore( ) 318.15 808.00 ± 0.50 −0.20 273.15 843.70 ± 0.50 −0.24 39-owe/qua(✕ ) 328.15 800.00 ± 0.50 −0.26 298.15 823.60 ± 0.50 −0.49 39-owe/qua(✕ ) 338.15 792.30 ± 0.50 −0.01 308.15 815.80 ± 0.50 −0.34 39-owe/qua(✕ )

1)

Ref. (Symbol in Fig. 1) 39-owe/qua(✕ ) 39-owe/qua(✕ ) 39-owe/qua(✕ )

Not included in Fig. 1.

cont. Landolt-Börnstein New Series IV/8G

206

2.1.7 Alkanols, C11 - C12

ρ

ρ

4-Methyl-4-decanol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15

ρ ± σ fit kg ⋅ m−3

ρ ± σ fit kg ⋅ m−3

T K

846.44 ± 0.98 838.50 ± 0.86 830.56 ± 0.72 828.06 ± 0.68

824.09 ± 0.61 822.62 ± 0.59 814.67 ± 0.49 806.73 ± 0.48

298.15 300.00 310.00 320.00

L-5-Methyl-1-decanol

[500001-17-2]

T K

330.00 340.00 350.00

C11H24O

ρ ± σ fit kg ⋅ m−3 798.79 ± 0.57 790.84 ± 0.78 782.90 ± 1.14

MW = 172.31

325

Table 1. Experimental value with uncertainty. T K

297.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

840.0 ± 2.0

33-lev/mar-1 Landolt-Börnstein New Series IV/8G

2.1.7 Alkanols, C11 - C12 5-Methyl-5-decanol

[87258-26-2]

207

C11H24O

MW = 172.31

326

C11H24O

MW = 172.31

327

C11H24O

MW = 172.31

328

C11H24O

MW = 172.31

329

C11H24O

MW = 172.31

330

C11H24O

MW = 172.31

331

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

298.15

Ref.

−3

kg ⋅ m

826.2 ± 1.0

33-whi/wil

l-6-Methyl-3-decanol

[900002-59-7]

Table 1. Experimental value with uncertainty. T K 297.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

829.0 ± 2.0

31-lev/mar-4

2-Methyl-3-(1-methylethyl)-3-heptanol

[5340-35-2]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est

T K

293.15 293.15 293.15 293.15 1)

Ref.

−3

kg ⋅ m

848.7 ± 1.0 855.7 ± 3.0 849.0 ± 1.0 848.9 ± 1.0

29-con/bla 43-geo1) 49-naz/pin Recommended

Not included in calculation of recommended value.

5-Methyl-3-(2-methylpropyl)-2-hexanol

[900002-62-2]

Table 1. Experimental value with uncertainty. T K 277.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

844.0 ± 2.0

10-fre

2-Methyl-4-propyl-4-heptanol

[56065-39-5]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

295.15

Ref.

−3

kg ⋅ m

831.1 ± 2.0

14-hal

4-Methyl-2-propyl-1-hexanol

[66256-62-0]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

kg ⋅ m−3

828.6 ± 1.0

Landolt-Börnstein New Series IV/8G

58-hag/hud

208

2.1.7 Alkanols, C11 - C12

4-(1-Methylethyl)-4-octanol

[900002-61-1]

C11H24O

MW = 172.31

332

C11H24O

MW = 172.31

333

C11H24O

MW = 172.31

334

C11H24O

MW = 172.31

335

C11H24O

MW = 172.31

336

C11H24O

MW = 172.31

337

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

840.0 ± 2.0

54-naz/kak-4

2,2,3,4,4-Pentamethyl-3-hexanol

[500000-99-7]

Table 1. Experimental value with uncertainty. T K

289.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

886.0 ± 2.0

37-naz

2,2,3,4,5-Pentamethyl-3-hexanol

[500000-98-6]

Table 1. Experimental value with uncertainty. T K

285.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

868.0 ± 2.0

37-naz

2,2,4,5,5-Pentamethyl-4-hexanol

[900002-64-4]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

841.0 ± 2.0

49-moe/whi

3,4,4,5,5-Pentamethyl-3-hexanol

[536-91-2]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

877.8 ± 2.0

60-pet/kao

3-Propyl-2-octanol

[500001-08-1]

Table 1. Experimental value with uncertainty. T K 290.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

831.0 ± 2.0

12-gue-2

Landolt-Börnstein New Series IV/8G

2.1.7 Alkanols, C11 - C12 4-Propyl-4-octanol

[6632-94-6]

C11H24O

209 MW = 172.31

338

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.100. Coefficient ρ = A + BT 1034.54 A B −0.680 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc ρexp ± 2σ est T Ref. −3 kg ⋅ m−3 K kg ⋅ m 293.15 33-whi/woo 835.1 ± 1.0 −0.10 298.15 0.10 33-whi/woo 831.9 ± 1.0 Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 290.00 837.3 ± 1.1 293.15 835.2 ± 0.9 298.15 831.8 ± 0.9 2,2,3,4-Tetramethyl-3-heptanol

[91337-08-5]

C11H24O

MW = 172.31

339

C 11H24O

MW = 172.31

340

C11H24O

MW = 172.31

341

C11H24O

MW = 172.31

342

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 273.15 37-naz 866.0 ± 2.0 2,2,3,6-Tetramethyl-3-heptanol

[106593-59-3]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 57-pet/sus 850.6 ± 1.0 2,2,4,6-Tetramethyl-4-heptanol

[106593-60-6]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 49-moe/whi 828.0 ± 2.0 2,3,4,4-Tetramethyl-3-heptanol

[91337-09-6]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 288.15 874.0 ± 2.0 37-naz Landolt-Börnstein New Series IV/8G

210

2.1.7 Alkanols, C11 - C12

2,2,4-Trimethyl-3-(1-methylethyl)3-pentanol

[5457-41-0]

C11H24O

MW = 172.31

343

[5340-54-5]

C11H24O

MW = 172.31

344

[42842-13-7]

C11H24O

MW = 172.31

345

[112-42-5]

C11H24O

MW = 172.31

346

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 292.15 293.15 293.15 1)

870.0 ± 2.0 875.8 ± 1.0 875.8 ± 1.0

46-vav/col1) 51-smi/cre Recommended

Not included in calculation of recommended value.

2,2,4-Trimethyl-4-octanol Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref.

K 293.15

kg ⋅ m−3

835.0 ± 1.0

49-moe/whi

2,4,7-Trimethyl-4-octanol Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref.

K 293.15

kg ⋅ m−3

825.0 ± 1.0

33-mey/tuo

1-Undecanol

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 2.5713 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.0106 · 10−1 (combined temperature ranges, unweighted).

T = 293.10 to 358.10 K ρ = A + BT + CT 2 + DT 3 + … 1.03691 · 103 −6.95763 · 10−1

Coefficient A B

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T

K 307.75 293.15 297.45 293.10 298.10 303.10 313.10 323.10 333.10 1)

−3

kg ⋅ m

821.68 ± 1.00 833.80 ± 1.00 829.80 ± 0.60 833.20 ± 0.40 829.80 ± 0.40 826.30 ± 0.40 819.40 ± 0.40 812.40 ± 0.40 805.20 ± 0.40

Not included in Fig. 1.

−3

kg ⋅ m

in Fig. 1)

−1.11 0.85 −0.16 0.22 0.29 0.27 0.33 0.29 0.05

27-ver/coo(✕ ) 42-mul(◆) 50-sac/sau(∇) 55-kus( ) 55-kus( ) 55-kus( ) 55-kus( ) 55-kus( ) 55-kus( )

K 343.10 353.10 358.10 298.15 308.15 318.15 333.15 298.15

−3

kg ⋅ m

798.30 ± 0.40 791.30 ± 0.40 787.70 ± 0.40 829.19 ± 0.30 822.36 ± 0.30 815.51 ± 0.30 804.95 ± 0.30 828.98 ± 0.60

kg ⋅ m

Ref. (Symbol in Fig. 1)

0.10 0.06 −0.06 −0.28 −0.15 −0.05 −0.17 −0.49

55-kus( ) 55-kus( ) 55-kus( ) 79-dia/tar( ) 79-dia/tar( ) 79-dia/tar( ) 79-dia/tar( ) 90-klo/pal(∆)

−3

cont. Landolt-Börnstein New Series IV/8G

2.1.7 Alkanols, C11 - C12

211

ρ

ρ

Further references: [03-bla/gue, 29-mah/das, 48-vog-2, 56-gol/kon, 63-vil/gav].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

290.00 293.15 298.15 300.00

ρ ± σ fit kg ⋅ m−3 835.14 ± 0.76 832.95 ± 0.69 829.47 ± 0.59 828.18 ± 0.56

2-Undecanol

ρ ± σ fit kg ⋅ m−3

T K

821.23 ± 0.42 814.27 ± 0.34 807.31 ± 0.32 800.35 ± 0.37

310.00 320.00 330.00 340.00

[1653-30-1]

T K

350.00 360.00 370.00

C11H24O

ρ ± σ fit kg ⋅ m−3 793.40 ± 0.47 786.44 ± 0.63 779.48 ± 0.84

MW = 172.31

347

Table 1. Fit with estimated B coefficient for 5 accepted points. Deviation σw = 1.587. Coefficient ρ = A + BT 1044.22 A B −0.740 cont.

Landolt-Börnstein New Series IV/8G

212

2.1.7 Alkanols, C11 - C12

2-Undecanol (cont.) Table 2. Experimental values with uncertainties and deviation from calculated values. T K

ρexp ± 2σ est

T K

Ref.

−3

kg ⋅ m

kg ⋅ m

292.15 826.8 ± 2.0 291.15 826.3 ± 2.0 296.15 827.0 ± 2.0 1)

ρexp − ρcalc

−3

−1.23 −2.47 1.93

1870-gie 03-tho/man 10-hal/las

ρexp ± 2σ est −3

kg ⋅ m

293.15 827.0 ± 1.0 405.15 739.3 ± 3.0 293.15 830.2 ± 2.0

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−0.29 −5.11 2.91

11-pic/ken 12-pic/ken1) 42-mul

Not included in calculation of linear coefficients.

Table 3. Recommended values. ρexp ± 2σ est

T K

kg ⋅ m−3

829.6 ± 2.1 827.3 ± 2.1 823.6 ± 2.1

290.00 293.15 298.15 3-Undecanol

[6929-08-4]

C11H24O

MW = 172.31

348

C11H24O

MW = 172.31

349

C11H24O

MW = 172.31

350

C12H26O

MW = 186.34

351

Table 1. Experimental values with uncertainties. T K

293.15 353.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

829.5 ± 2.0 782.7 ± 2.0

13-pic/ken 13-pic/ken

4-Undecanol

[4272-06-4]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

821.5 ± 1.0

65-das/mae

6-Undecanol

[23708-56-7]

Table 1. Experimental values with uncertainties. T K

293.15 294.95

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

833.4 ± 2.0 827.2 ± 2.0

25-hes/bap 25-hes/bap

3-Butyl-3-methyl-2-heptanol

[500001-77-4]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

850.0 ± 2.0

33-whi/kru

Landolt-Börnstein New Series IV/8G

2.1.7 Alkanols, C11 - C12 2-Butyl-1-octanol

[3913-02-8]

213

C12H26O

MW = 186.34

352

C12H26O

MW = 186.34

353

C12H26O

MW = 186.34

354

C12H26O

MW = 186.34

355

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.255. Coefficient ρ = A + BT 1051.19 A B −0.740 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

289.65 293.15

−3

kg ⋅ m

837.1 ± 1.0 834.0 ± 1.0

ρexp − ρcalc

Ref.

kg ⋅ m−3

0.25 −0.26

38-mas 53-ano-15

Table 3. Recommended values. ρexp ± 2σ est

T K 280.00 290.00 293.15 298.15

kg ⋅ m−3

844.0 ± 1.1 836.6 ± 0.9 834.3 ± 0.9 830.6 ± 1.0

4-Butyl-1-octanol

[500001-73-0]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

289.15

Ref.

kg ⋅ m−3

841.0 ± 2.0

16-lev/all

2,4-Diethyl-1-octanol

[55514-25-5]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

840.0 ± 1.0

61-mil/ben

2,2-Dimethyl-1-decanol

[2370-15-2]

Table 1. Experimental values with uncertainties. T K 293.15 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

834.5 ± 2.0 839.0 ± 2.0

Landolt-Börnstein New Series IV/8G

64-blo/hag 65-shu/puz

214

2.1.7 Alkanols, C11 - C12

2,4-Dimethyl-4-decanol

[106652-28-2]

C12H26O

MW = 186.34

356

C12H26O

MW = 186.34

357

C12H26O

MW = 186.34

358

C12H26O

MW = 186.34

359

C12H26O

MW = 186.34

360

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 59-pet/zak 828.4 ± 2.0 3,5-Dimethyl-5-decanol

[105900-70-7]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 301.15 60-tha/vas 827.0 ± 1.0 5,9-Dimethyl-5-decanol

[900002-66-6]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 284.15 28-esc 852.6 ± 2.0 6,6-Dimethyl-5-decanol

[500001-68-3]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 33-whi/kru 845.0 ± 2.0 2,2-Dimethyl-3-(1,1-dimethylethyl)3-hexanol

[32579-69-4]

Table 1. Experimental and recommended values with uncertainties. T K 293.15 293.15 1)

ρexp ± 2σ est

T K 293.15 293.15

Ref.

kg ⋅ m−3

859.5 ± 1.0 895.5 ± 3.0

48-cad/foo 51-smi/cre1)

ρexp ± 2σ est

Ref.

kg ⋅ m−3

865.2 ± 3.0 859.5 ± 1.0

57-pet/sok1) Recommended

Not included in calculation of recommended value.

5,5-Dimethyl-4-(1,1-dimethylethyl)1-hexanol

[900002-67-7]

C12H26O

MW = 186.34

361

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 60-pet/sok 865.2 ± 2.0

Landolt-Börnstein New Series IV/8G

2.1.7 Alkanols, C11 - C12 2,2-Dimethyl-4-ethyl-3-octanol

[124154-63-8]

215

C12H26O

MW = 186.34

362

C12H26O

MW = 186.34

363

C12H26O

MW = 186.34

364

C12H26O

MW = 186.34

365

C12H26O

MW = 186.34

366

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

840.9 ± 1.0

41-whi/whi

2,2-Dimethyl-3-(1-methylethyl)3-heptanol

[500001-78-5]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

−3

kg ⋅ m

856.5 ± 1.0

50-naz/kot-1

2,6-Dimethyl-3-(1-methylethyl)3-heptanol

[5340-82-9]

Table 1. Experimental values with uncertainties. T K 289.15 273.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

860.6 ± 2.0 871.7 ± 2.0

14-mur/amo 14-mur/amo

2,2-Dimethyl-4-propyl-4-heptanol

[500001-79-6]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est

T K

293.15 293.15 293.15

Ref.

kg ⋅ m−3

837.6 ± 1.0 838.6 ± 1.0 838.1 ± 1.1

1-Dodecanol

8 -whi/pop -1 2 -whi/for -0 Recommended

[112-53-8]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 2.7829 · 10−1 (combined temperature ranges, weighted), σc,uw = 9.5525 · 10−2 (combined temperature ranges, unweighted). Coefficient A B C D

T = 296.90 to 533.15 K ρ = A + BT + CT 2 + DT 3 + … 9.42675 · 102 −4.51517 · 10−2 −1.31349 · 10−3 6.54515 · 10−7 cont.

Landolt-Börnstein New Series IV/8G

216

2.1.7 Alkanols, C11 - C12

1-Dodecanol (cont.) Table 2. Experimental values with uncertainties and deviation from calculated values. T K

ρexp ± 2σ est −3

kg ⋅ m

crystal 78.15 1017.0 ± 3.0 194.15 981.0 ± 3.0 liquid 297.15 830.90 ± 1.00 313.15 820.10 ± 1.00 372.15 778.10 ± 1.00 313.15 819.60 ± 0.60 333.15 805.70 ± 0.60 353.15 792.00 ± 0.60 373.15 777.40 ± 0.60 393.15 762.20 ± 0.60 413.15 746.80 ± 1.00 433.15 730.70 ± 1.00 453.15 714.40 ± 1.00 473.15 698.20 ± 1.00 493.15 681.00 ± 1.00 513.15 663.50 ± 1.50 533.15 645.70 ± 1.50 553.15 627.50 ± 1.50 573.15 609.70 ± 1.50 293.15 834.60 ± 1.00 298.15 831.20 ± 1.00 303.15 827.80 ± 1.00 308.15 824.40 ± 1.00 313.15 821.10 ± 1.00 318.15 817.80 ± 1.00 323.15 814.40 ± 1.00 328.15 811.00 ± 1.00 333.15 807.50 ± 1.00 338.15 804.00 ± 1.00 343.15 800.20 ± 1.00 348.15 796.50 ± 1.00 353.15 792.80 ± 1.00 358.15 789.00 ± 1.00 363.15 785.20 ± 1.00 296.90 830.62 ± 0.20 297.89 829.95 ± 0.20 298.78 829.36 ± 0.20 1)

ρexp − ρcalc −3

kg ⋅ m

Ref. (Symbol in Fig. 1) 30-bil/fis-1 30-bil/fis-1

0.45 0.27 0.41 −0.23 −0.35 0.26 0.46 0.53 0.83 0.83 1.00 1.61 1.53 1.43 1.27 0.92 1.16 1.55 1.40 1.29 1.21 1.27 1.36 1.39 1.45 1.45 1.48 1.24 1.13 1.06 0.91 0.80 0.00 −0.02 −0.03

1883-kra1) 1883-kra1) 1883-kra(✕ ) 58-cos/bow1) 58-cos/bow1) 58−cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow1) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow1) 58-cos/bow1) 62-gei/qui1) 62-gei/qui1) 62-gei/qui1) 62-gei/qui1) 62-gei/qui1) 62-gei/qui1) 62-gei/qui1) 62-gei/qui1) 62-gei/qui1) 62-gei/qui1) 62-gei/qui1) 62-gei/qui1) 62-gei/qui1) 62-gei/qui(✕ ) 62-gei/qui(✕ ) 73-fin(✕ ) 73-fin(✕ ) 73-fin(✕ )

T K

303.14 313.13 323.07 333.20 298.15 303.15 320.00 340.00 360.00 380.00 400.00 420.00 440.00 460.00 470.00 480.00 490.00 298.15 303.15 308.15 298.15 308.15 318.15 333.15 298.15 333.15 298.15 303.15 308.15 313.15 318.15 323.15 328.15 333.15 338.15 343.15 348.15 353.15

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

826.39 ± 0.20 819.60 ± 0.20 812.78 ± 0.20 805.77 ± 0.20 829.65 ± 0.25 826.20 ± 0.25 814.81 ± 0.25 800.96 ± 0.25 786.54 ± 0.25 771.73 ± 0.30 756.33 ± 0.30 740.41 ± 0.30 724.02 ± 0.30 707.21 ± 0.30 698.99 ± 0.35 689.99 ± 0.35 681.24 ± 0.35 830.00 ± 0.20 826.57 ± 0.20 823.16 ± 0.20 829.95 ± 0.30 823.20 ± 0.30 816.33 ± 0.30 806.06 ± 0.30 823.00 ± 0.40 805.81 ± 0.40 828.50 ± 0.60 825.50 ± 0.60 822.50 ± 0.60 818.20 ± 0.60 815.20 ± 0.60 811.90 ± 0.60 809.00 ± 0.60 804.70 ± 0.60 801.50 ± 0.60 798.40 ± 0.60 794.20 ± 0.60 790.90 ± 0.60

−0.13 −0.24 −0.28 −0.25 −0.15 −0.31 −0.36 −0.25 −0.19 −0.03 −0.01 −0.09 −0.25 −0.47 −0.27 −0.77 −0.94 0.20 0.06 −0.03 0.15 0.01 −0.11 0.01 −6.80 −0.24 −1.30 −1.01 −0.69 −1.63 −1.24 −1.11 −0.55 −1.35 −1.02 −0.56 −1.17 −0.84

kg ⋅ m

Ref. (Symbol in Fig. 1) 73-fin(✕ ) 73-fin(✕ ) 73-fin(✕ ) 73-fin(✕ ) 76-hal/ell( ) 76-hal/ell( ) 76-hal/ell( ) 76-hal/ell( ) 76-hal/ell( ) 76-hal/ell( ) 76-hal/ell( ) 76-hal/ell( ) 76-hal/ell( ) 76-hal/ell( ) 76-hal/ell( ) 76-hal/ell( ) 76-hal/ell( ) 78-jel/leo( ) 78-jel/leo( ) 78-jel/leo( ) 79-dia/tar(∆) 79-dia/tar(∆) 79-dia/tar(∆) 79-dia/tar(∆) 86-wag/hei1) 86-wag/hei(∇) 92-lie/sen-11) 92-lie/sen-11) 92-lie/sen-11) 92-lie/sen-11) 92-lie/sen-11) 92-lie/sen-1(◆) 92-lie/sen-1(◆) 92-lie/sen-11) 92-lie/sen-1(◆) 92-lie/sen-1(◆) 92-lie/sen-1(◆) 92-lie/sen-1(◆)

Not included in Fig. 1.

Further references: [27-ver/coo, 29-mah/das, 31-zaa, 36-pal/sab, 42-mul, 43-hsu, 44-sto/rou, 46-par/row, 48-wei, 49-tsv/mar, 50-sac/sau, 55-pet/sus, 56-rat/cur, 63-vil/gav, 67-seu/mor, 93-yan/mae]. cont. Landolt-Börnstein New Series IV/8G

217

ρ

ρ

2.1.7 Alkanols, C11 - C12

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

290.00 293.15 298.15 300.00 310.00 320.00 330.00 340.00 350.00 360.00

Landolt-Börnstein New Series IV/8G

ρ ± σ fit kg ⋅ m−3 835.08 ± 0.60 833.05 ± 0.59 829.80 ± 0.59 828.59 ± 0.59 821.95 ± 0.58 815.17 ± 0.58 808.26 ± 0.58 801.21 ± 0.58 794.03 ± 0.60 786.73 ± 0.60

T K

370.00 380.00 390.00 400.00 410.00 420.00 430.00 440.00 450.00 460.00

ρ ± σ fit kg ⋅ m−3 779.30 ± 0.59 771.76 ± 0.56 764.11 ± 0.53 756.34 ± 0.50 748.47 ± 0.47 740.50 ± 0.45 732.43 ± 0.44 724.27 ± 0.45 716.02 ± 0.47 707.68 ± 0.52

T K

470.00 480.00 490.00 500.00 510.00 520.00 530.00 540.00

ρ ± σ fit kg ⋅ m−3 699.26 ± 0.60 690.76 ± 0.72 682.18 ± 0.88 673.54 ± 1.09 664.83 ± 1.36 656.06 ± 1.69 647.23 ± 2.08 638.34 ± 2.53

218

2.1.7 Alkanols, C11 - C12

2-Dodecanol

[10203-28-8]

C12H26O

MW = 186.34

367

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 1.0204 · 10−1 (combined temperature ranges, weighted), σc,uw = 2.8302 · 10−2 (combined temperature ranges, unweighted). T = 293.15 to 363.15 K ρ = A + BT + CT 2 + DT 3 + … 9.76605 · 102 −3.16820 · 10−1 −6.34131 · 10−4

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 293.15 298.15 303.15 308.15 313.15 318.15 323.15 328.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

829.30 ± 1.00 825.80 ± 1.00 822.30 ± 1.00 818.70 ± 1.00 815.10 ± 1.00 811.50 ± 1.00 808.00 ± 1.00 804.60 ± 1.00

0.07 0.02 0.02 −0.06 −0.11 −0.12 −0.01 0.24

Ref. (Symbol in Fig. 1) 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui(

) ) ) ) ) ) ) )

T K 333.15 338.15 343.15 348.15 353.15 358.15 363.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

800.60 ± 1.00 796.90 ± 1.00 793.30 ± 1.00 789.40 ± 1.00 785.80 ± 1.00 781.80 ± 1.00 777.80 ± 1.00

−0.08 −0.06 0.08 −0.04 0.17 0.00 −0.12

Ref. (Symbol in Fig. 1) 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui(

) ) ) ) ) ) )

Further references: [11-pic/ken].

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

290.00 293.15 298.15 300.00

ρ ± σ fit kg ⋅ m−3 831.40 ± 1.45 829.23 ± 1.36 825.78 ± 1.24 824.49 ± 1.20

T K

310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 817.45 ± 1.05 810.29 ± 0.97 803.00 ± 0.92 795.58 ± 0.92

T K

350.00 360.00 370.00

ρ ± σ fit kg ⋅ m−3 788.04 ± 1.05 780.37 ± 1.37 772.57 ± 1.94

cont. Landolt-Börnstein New Series IV/8G

219

ρ

ρ

2.1.7 Alkanols, C11 - C12

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

3-Dodecanol

[10203-30-2]

C12H26O

MW = 186.34

368

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 3.8100 · 10−2 (combined temperature ranges, weighted), σc,uw = 1.0998 · 10−2 (combined temperature ranges, unweighted). T = 293.15 to 363.15 K ρ = A + BT + CT 2 + DT 3 + … 1.00182 · 103 −4.39256 · 10−1 −4.82504 · 10−4

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 293.15 298.15 303.15

ρexp ± 2σ est

ρexp − ρcalc

−3

kg ⋅ m

Ref. (Symbol in Fig. 1)

831.60 ± 1.00 828.00 ± 1.00 824.30 ± 1.00

0.01 0.03 −0.02

62-gei/qui( ) 62-gei/qui( ) 62-gei/qui( )

kg ⋅ m

−3

T K 308.15 313.15 318.15

ρexp ± 2σ est

ρexp − ρcalc

−3

kg ⋅ m

Ref. (Symbol in Fig. 1)

820.60 ± 1.00 816.90 ± 1.00 813.30 ± 1.00

−0.05 −0.05 0.06

62-gei/qui( ) 62-gei/qui( ) 62-gei/qui( )

kg ⋅ m

−3

cont. Landolt-Börnstein New Series IV/8G

220

2.1.7 Alkanols, C11 - C12

3-Dodecanol (cont.) Table 2. (cont.) T K 323.15 328.15 333.15 338.15 343.15 1)

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

809.70 ± 1.00 805.80 ± 1.00 801.90 ± 1.00 798.10 ± 1.00 794.30 ± 1.00

0.21 0.08 −0.03 −0.02 0.02

kg ⋅ m

Ref. (Symbol in Fig. 1) 62-gei/qui1) 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui(

) ) ) )

T K 348.15 353.15 358.15 363.15

ρexp ± 2σ est

ρexp − ρcalc kg ⋅ m−3

−3

kg ⋅ m

790.40 ± 1.00 786.50 ± 1.00 782.60 ± 1.00 778.70 ± 1.00

−0.01 −0.03 −0.01 0.02

Ref. (Symbol in Fig. 1) 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui(

) ) ) )

Not included in Fig. 1.

ρ

ρ

Further references: [13-pic/ken].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

290.00 293.15 298.15 300.00

ρ ± σ fit kg ⋅ m−3 833.86 ± 1.45 831.59 ± 1.36 827.97 ± 1.23 826.62 ± 1.20

T K

310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 819.29 ± 1.05 811.85 ± 0.96 804.32 ± 0.92 796.70 ± 0.92

T K

350.00 360.00 370.00

ρ ± σ fit kg ⋅ m−3 788.98 ± 1.04 781.16 ± 1.37 773.24 ± 1.96

Landolt-Börnstein New Series IV/8G

2.1.7 Alkanols, C11 - C12 4-Dodecanol

[10203-32-4]

221

C12H26O

MW = 186.34

369

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 4.1061 · 10−2 (combined temperature ranges, weighted), σc,uw = 1.1853 · 10−2 (combined temperature ranges, unweighted). T = 293.15 to 363.15 K ρ = A + BT + CT 2 + DT 3 + … 9.85212 · 102 −3.51028 · 10−1 −6.18755 · 10−4

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

293.15 298.15 303.15 308.15 313.15 318.15 323.15 328.15 1)

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

829.20 ± 1.00 825.50 ± 1.00 821.90 ± 1.00 818.30 ± 1.00 814.60 ± 1.00 810.90 ± 1.00 807.30 ± 1.00 803.40 ± 1.00

0.07 −0.05 −0.03 0.01 −0.01 −0.00 0.14 0.01

kg ⋅ m

Ref. (Symbol in Fig. 1)

) ) ) ) ) ) )

62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui1) 62-gei/qui(

T K

333.15 338.15 343.15 348.15 353.15 358.15 363.15

ρexp ± 2σ est

ρexp − ρcalc −3

−3

kg ⋅ m

799.60 ± 1.00 795.70 ± 1.00 791.90 ± 1.00 788.10 ± 1.00 784.10 ± 1.00 780.10 ± 1.00 776.10 ± 1.00

0.01 −0.06 0.00 0.10 0.02 −0.02 −0.04

kg ⋅ m

Ref. (Symbol in Fig. 1) 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui(

) ) ) ) ) ) )

Not included in Fig. 1.

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

290.00 293.15 298.15 300.00

ρ ± σ fit kg ⋅ m−3 831.38 ± 1.45 829.13 ± 1.36 825.55 ± 1.23 824.22 ± 1.20

T K

310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 816.93 ± 1.05 809.52 ± 0.96 801.99 ± 0.92 794.33 ± 0.92

T K

350.00 360.00 370.00

ρ ± σ fit kg ⋅ m−3 786.55 ± 1.04 778.65 ± 1.37 770.62 ± 1.96

cont. Landolt-Börnstein New Series IV/8G

222

2.1.7 Alkanols, C11 - C12

ρ

ρ

4-Dodecanol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

5-Dodecanol

[10203-33-5]

C12H26O

MW = 186.34

370

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 7.5305 · 10−2 (combined temperature ranges, weighted), σc,uw = 2.1739 · 10−2 (combined temperature ranges, unweighted). T = 293.15 to 363.15 K ρ = A + BT + CT 2 + DT 3 + … 9.59772 · 102 −1.92462 · 10−1 −8.58906 · 10−4

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

ρexp ± 2σ est −3

kg ⋅ m

293.15 829.50 ± 1.00 298.15 826.00 ± 1.00 303.15 822.50 ± 1.00

ρexp − ρcalc kg ⋅ m

Ref. (Symbol in Fig. 1)

−0.04 −0.04 0.01

62-gei/qui( ) 62-gei/qui( ) 62-gei/qui( )

−3

T K

ρexp ± 2σ est −3

kg ⋅ m

308.15 818.90 ± 1.00 313.15 815.40 ± 1.00 318.15 811.70 ± 1.00

ρexp − ρcalc kg ⋅ m

Ref. (Symbol in Fig. 1)

−0.01 0.12 0.10

62-gei/qui( ) 62-gei/qui( ) 62-gei/qui( )

−3

cont. Landolt-Börnstein New Series IV/8G

2.1.7 Alkanols, C11 - C12

223

Table 2. (cont.) ρexp ± 2σ est

T K

807.90 ± 1.00 804.10 ± 1.00 800.30 ± 1.00 796.30 ± 1.00 792.30 ± 1.00

0.01 −0.03 −0.02 −0.18 −0.29

Ref. (Symbol in Fig. 1)

) ) ) )

62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui1)

T K

348.15 353.15 358.15 363.15

ρexp ± 2σ est

ρexp − ρcalc kg ⋅ m−3

−3

kg ⋅ m

788.60 ± 1.00 784.80 ± 1.00 780.70 ± 1.00 776.60 ± 1.00

−0.06 0.11 0.03 −0.01

Ref. (Symbol in Fig. 1) 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui(

) ) ) )

Not included in Fig. 1.

ρ

ρ

1)

−3

kg ⋅ m

kg ⋅ m

323.15 328.15 333.15 338.15 343.15

ρexp − ρcalc

−3

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

290.00 293.15 298.15 300.00

Landolt-Börnstein New Series IV/8G

ρ ± σ fit kg ⋅ m−3 831.72 ± 1.45 829.54 ± 1.36 826.04 ± 1.24 824.73 ± 1.21

T K

310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 817.57 ± 1.05 810.23 ± 0.96 802.73 ± 0.91 795.05 ± 0.92

T K

350.00 360.00 370.00

ρ ± σ fit kg ⋅ m−3 787.19 ± 1.03 779.17 ± 1.36 770.98 ± 1.95

224

2.1.7 Alkanols, C11 - C12

6-Dodecanol

[6836-38-0]

C12H26O

MW = 186.34

371

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 8.7855 · 10−2 (combined temperature ranges, weighted), σc,uw = 2.6489 · 10−2 (combined temperature ranges, unweighted). Coefficient A B C

T = 303.15 to 363.15 K ρ = A + BT + CT 2 + DT 3 + … 9.92440 · 102 −4.06419 · 10−1 −5.33467 · 10−4

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

820.10 ± 1.00 816.50 ± 1.00 812.90 ± 1.00 809.30 ± 1.00 805.50 ± 1.00 801.70 ± 1.00 797.80 ± 1.00

−0.11 −0.05 0.04 0.16 0.10 0.07 −0.03

Ref. (Symbol in Fig. 1) 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui(

) ) ) ) ) ) )

T K

338.15 343.15 348.15 353.15 358.15 363.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

793.90 ± 1.00 790.10 ± 1.00 786.20 ± 1.00 782.30 ± 1.00 778.50 ± 1.00 774.60 ± 1.00

−0.11 −0.06 −0.08 −0.08 0.05 0.10

Ref. (Symbol in Fig. 1) 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui( 62-gei/qui(

) ) ) ) ) )

ρ

ρ

303.15 308.15 313.15 318.15 323.15 328.15 333.15

ρexp ± 2σ est

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.).

cont.

Landolt-Börnstein New Series IV/8G

2.1.7 Alkanols, C11 - C12

225

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ).

ρ ± σ fit kg ⋅ m−3

T K

822.50 ± 1.50 815.18 ± 1.19 807.76 ± 1.02

300.00 310.00 320.00

ρ ± σ fit kg ⋅ m−3

T K

800.23 ± 0.94 792.59 ± 0.92 784.84 ± 1.00

330.00 340.00 350.00

5-Ethyl-5-decanol

[91635-39-1]

T K

360.00 370.00

C12H26O

ρ ± σ fit kg ⋅ m−3 776.99 ± 1.35 769.03 ± 2.03

MW = 186.34

372

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 1.122. Coefficient ρ = A + BT 1054.83 A B −0.740 Table 2. Experimental values with uncertainties and deviation from calculated values. T K 298.15 318.15 328.15

ρexp ± 2σ est

ρexp − ρcalc

Ref.

kg ⋅ m−3

−3

kg ⋅ m

835.7 ± 1.0 819.1 ± 1.0 810.8 ± 1.0

1.50 −0.30 −1.20

44-qua/sma 44-qua/sma 44-qua/sma

Table 3. Recommended values. ρexp ± 2σ est

T K 290.00 293.15

ρexp ± 2σ est

T K 298.15 310.00

−3

kg ⋅ m

840.2 ± 1.9 837.9 ± 1.8

6-Ethyl-3-decanol

−3

kg ⋅ m

834.2 ± 1.7 825.4 ± 1.5

[19780-31-5]

T K 320.00 330.00

ρexp ± 2σ est kg ⋅ m−3

818.0 ± 1.5 810.6 ± 1.6

C12H26O

MW = 186.34

373

C12H26O

MW = 186.34

374

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

301.15

Ref.

−3

kg ⋅ m

836.4 ± 1.0

36-pow/bal

4-Ethyl-2-methyl-3-(1-methylethyl)3-hexanol

[500001-86-5]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

−3

kg ⋅ m

852.8 ± 1.0

Landolt-Börnstein New Series IV/8G

43-geo

226

2.1.7 Alkanols, C11 - C12

5-Ethyl-2-methyl-3-nonanol

[105902-95-2]

C12H26O

MW = 186.34

375

C12H26O

MW = 186.34

376

C12H26O

MW = 186.34

377

C12H26O

MW = 186.34

378

C12H26O

MW = 186.34

379

C12H26O

MW = 186.34

380

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

847.1 ± 2.0

57-pet/nef-1

5-Ethyl-7-methyl-3-nonanol

[66634-87-5]

Table 1. Experimental value with uncertainty. T K 273.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

921.0 ± 2.0

12-gue

4-Ethyl-2,2,3,4-tetramethyl-3-hexanol

[91635-45-9]

Table 1. Experimental value with uncertainty. T K

291.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

892.0 ± 2.0

37-naz

3-Ethyl-3,4,5-trimethyl-4-heptanol

[500002-61-9]

Table 1. Experimental value with uncertainty. T K 286.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

885.0 ± 2.0

37-naz

2,2,3,4,4,5-Hexamethyl-3-hexanol

[500002-63-1]

Table 1. Experimental value with uncertainty. T K

286.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

893.0 ± 2.0

37-naz

2,2,4,4,5,5-Hexamethyl-3-hexanol

[500001-88-7]

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 0.245. Coefficient ρ = A + BT 1065.31 A B −0.700 cont. Landolt-Börnstein New Series IV/8G

2.1.7 Alkanols, C11 - C12

227

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 288.15 293.15 303.15 313.15 1)

ρexp ± 2σ est −3

kg ⋅ m

848.1 ± 4.0 860.4 ± 0.6 853.1 ± 0.6 845.8 ± 0.6

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−15.50 0.30 −0.00 −0.30

33-fav/naz1) 53-per/wag 53-per/wag 53-per/wag

Not included in calculation of linear coefficients.

Table 3. Recommended values. ρexp ± 2σ est

T K 290.00 293.15 298.15 310.00 320.00

kg ⋅ m−3

862.3 ± 0.8 860.1 ± 0.7 856.6 ± 0.5 848.3 ± 0.6 841.3 ± 1.0

2,3,4,4,5,5-Hexamethyl-3-hexanol

[100392-68-5]

C12H26O

MW = 186.34

381

C12H26O

MW = 186.34

382

C12H26O

MW = 186.34

383

C12H26O

MW = 186.34

384

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

888.6 ± 2.0

60-pet/kao

5-Methyl-2-(3-methylbutyl)-1-hexanol

[500001-82-1]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

−3

kg ⋅ m

834.0 ± 1.0

37-bra/kur

2-Methyl-3-(1-methylethyl)-3-octanol

[19965-71-0]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

−3

kg ⋅ m

853.7 ± 1.0

43-geo

5-Methyl-5-propyl-4-octanol

[500001-75-2]

Table 1. Experimental value with uncertainty. T K 289.65

ρexp ± 2σ est

Ref.

kg ⋅ m−3

845.5 ± 1.0

Landolt-Börnstein New Series IV/8G

21-ler

228

2.1.7 Alkanols, C11 - C12

2-Methyl-2-undecanol

[32836-42-3]

C12H26O

MW = 186.34

385

C12H26O

MW = 186.34

386

C12H26O

MW = 186.34

387

C12H26O

MW = 186.34

388

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.410. Coefficient ρ = A + BT 1046.24 A B −0.740 Table 2. Experimental values with uncertainties and deviation from calculated values. T K

273.15 286.15

ρexp ± 2σ est −3

kg ⋅ m

843.7 ± 1.0 834.9 ± 1.0

ρexp − ρcalc

Ref.

kg ⋅ m−3

−0.41 0.41

19-beh 19-beh

Table 3. Recommended values. T K 270.00 280.00 290.00

ρexp ± 2σ est kg ⋅ m−3

846.4 ± 1.1 839.0 ± 1.0 831.6 ± 1.1

2-Methyl-3-undecanol

[60671-36-5]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

832.7 ± 2.0

12-pic/ken

2-Methyl-5-undecanol

[33978-71-1]

Table 1. Experimental values with uncertainties. T K

293.15 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

826.6 ± 1.0 825.1 ± 2.0

3-Methyl-1-undecanol

44-pow/hag 48-pet/old

[71526-27-7]

Table 1. Fit with estimated B coefficient for 4 accepted points. Deviation σw = 0.817. Coefficient ρ = A + BT 1039.61 A B −0.700 cont.

Landolt-Börnstein New Series IV/8G

2.1.7 Alkanols, C11 - C12

229

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 293.15 298.15 303.15 308.15

ρexp ± 2σ est

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−3

kg ⋅ m

834.1 ± 1.0 830.9 ± 1.0 827.5 ± 1.0 824.1 ± 1.0

−0.30 −0.00 0.10 0.20

48-pro/cas 48-pro/cas 48-pro/cas 48-pro/cas

Table 3. Recommended values. ρexp ± 2σ est

T K

kg ⋅ m−3

836.6 ± 1.1 834.4 ± 1.0 830.9 ± 0.9 822.6 ± 1.0

290.00 293.15 298.15 310.00

[S-(R*,R*)]-3-Methyl-5-undecanol

[82749-56-2]

C12H26O

MW = 186.34

389

C12H26O

MW = 186.34

390

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

297.15

Ref.

−3

kg ⋅ m

827.2 ± 2.0

35-lev/har

5-Methyl-5-undecanol

[21078-80-8]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 3.2352 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.4468 · 10−1 (combined temperature ranges, unweighted). Coefficient A B

T = 273.15 to 338.15 K ρ = A + BT + CT 2 + DT 3 + … 1.05408 · 103 −7.68000 · 10−1

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

273.15 844.70 ± 1.00 298.15 824.70 ± 1.00 308.15 817.00 ± 1.00

0.40 −0.40 −0.42

Ref. (Symbol in Fig. 1)

T K

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

39-owe/qua( ) 318.15 809.70 ± 1.00 39-owe/qua( ) 328.15 802.40 ± 1.00 39-owe/qua( ) 338.15 794.50 ± 1.00

−0.04 0.34 0.12

Ref. (Symbol in Fig. 1)

39-owe/qua( ) 39-owe/qua( ) 39-owe/qua( )

cont.

Landolt-Börnstein New Series IV/8G

230

2.1.7 Alkanols, C11 - C12

ρ

ρ

5-Methyl-5-undecanol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15

ρ ± σ fit kg ⋅ m−3

ρ ± σ fit kg ⋅ m−3

T K

846.72 ± 1.53 839.04 ± 1.35 831.36 ± 1.15 828.94 ± 1.08

825.10 ± 0.99 823.68 ± 0.96 816.00 ± 0.86 808.32 ± 0.90

298.15 300.00 310.00 320.00

6-Methyl-6-undecanol

[5340-31-8]

T K

330.00 340.00 350.00

C12H26O

ρ ± σ fit kg ⋅ m−3 800.64 ± 1.13 792.96 ± 1.58 785.28 ± 2.26

MW = 186.34

391

Table 1. Experimental value with uncertainty. T K

298.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

827.1 ± 1.0

33-whi/wil

Landolt-Börnstein New Series IV/8G

2.1.7 Alkanols, C11 - C12 9-Methyl-1-undecanol

[91635-46-0]

231

C12H26O

MW = 186.34

392

C12H26O

MW = 186.34

393

C12H26O

MW = 186.34

394

C12H26O

MW = 186.34

395

C12H26O

MW = 186.34

396

C12H26O

MW = 186.34

397

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

831.6 ± 1.0

62-lar/sal

L(+)-9-Methyl-1-undecanol

[500006-92-8]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

298.15

Ref.

kg ⋅ m−3

831.6 ± 0.6

62-lar/sal

5-(1-Methylethyl)-5-nonanol

[76144-88-2]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

kg ⋅ m−3

844.0 ± 2.0

33-whi/kru

3-(1-Methylethyl)-2,2,4,4-tetramethyl3-pentanol

[5457-42-1]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est

T K

293.15 293.15 293.15

Ref.

kg ⋅ m−3

888.9± 1.0 885.3 ± 2.0 888.2 ± 1.6

51-smi/cre 57-pet/sok Recommended

3-(1-Methylethyl)-2,2,5-trimethyl-3hexanol

[500001-89-8]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

kg ⋅ m−3

855.2 ± 2.0

57-pet/sus

2,2,3,3,4-Pentamethyl-4-heptanol

[500001-81-0]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

−3

kg ⋅ m

877.2 ± 2.0

Landolt-Börnstein New Series IV/8G

60-pet/kao

232

2.1.7 Alkanols, C11 - C12

2,2,4,6,6-Pentamethyl-3-heptanol

[105902-93-0]

C12H26O

MW = 186.34

398

C12H26O

MW = 186.34

399

C12H26O

MW = 186.34

400

C12H26O

MW = 186.34

401

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

838.0 ± 1.0

41-whi/whi

4-Propyl-4-nonanol

[5340-77-2]

Table 1. Experimental value with uncertainty. T K 297.65

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

832.4 ± 2.0

33-whi/wil

5-Propyl-5-nonanol

[5340-52-3]

Table 1. Fit with estimated B coefficient for 4 accepted points. Deviation σw = 1.052. Coefficient ρ = A + BT 1066.88 A B −0.780 Table 2. Experimental values with uncertainties and deviation from calculated values. T K

293.15 298.15 288.15 293.15

ρexp ± 2σ est −3

kg ⋅ m

837.0 ± 2.0 834.0 ± 2.0 842.0 ± 2.0 839.9 ± 2.0

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−1.23 −0.33 −0.13 1.67

33-whi/woo 33-whi/woo 37-pet/mal 61-mes/erz

Table 3. Recommended values. T K

280.00 290.00 293.15 298.15

ρexp ± 2σ est kg ⋅ m−3

848.5 ± 2.5 840.7 ± 2.1 838.2 ± 2.1 834.3 ± 2.1

2,2,3,4,4-Pentamethyl-3-heptanol

[500002-60-8]

Table 1. Experimental value with uncertainty. T K

286.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

885.0 ± 2.0

37-naz Landolt-Börnstein New Series IV/8G

2.1.7 Alkanols, C11 - C12 2,2,5,6,6-Pentamethyl-3-heptanol

[500002-65-3]

233

C12H26O

MW = 186.34

402

C 12H26O

MW = 186.34

403

C12H26O

MW = 186.34

404

C12H26O

MW = 186.34

405

C12H26O

MW = 186.34

406

C12H26O

MW = 186.34

407

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

289.15

Ref.

−3

kg ⋅ m

845.0 ± 2.0

35-col

3,3,4,5,5-Pentamethyl-4-heptanol

[500002-62-0]

Table 1. Experimental value with uncertainty. T K 289.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

900.4 ± 1.0

37-naz

2,5,8-Trimethyl-5-nonanol

[64029-94-3]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

828.9 ± 1.0

59-yur/bel

2,6,8-Trimethyl-4-nonanol

[123-17-1]

Table 1. Experimental value with uncertainty. T K 293.15 293.15 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

817.9 ± 1.0 817.9 ± 1.0 817.9 ± 1.0

53-ano-15 58-ano-5 68-ano

3,4,8-Trimethyl-1-nonanol

[18352-71-1]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

846.3 ± 1.0

67-min/che

3,4,8-Trimethyl-3-nonanol

[18352-67-5]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

836.6 ± 1.0

Landolt-Börnstein New Series IV/8G

67-min/che

2.1.8 Alkanols, C13 - C22

235

2.1.8 Alkanols, C13 - C22 3-Butyl-2,2-dimethyl-3-heptanol

[900002-68-8]

C13H28O

MW = 200.36

408

C13H28O

MW = 200.36

409

C13H28O

MW = 200.36

410

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

849.8 ± 1.0

38-whi/pop

2-Butyl-1-nonanol

[51655-57-3]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

kg ⋅ m−3

835.9 ± 2.0

22-lev/tay-1

5-Butyl-5-nonanol

[597-93-3]

Table 1. Experimental and recommended values with uncertainties. T K 295.85 351.85 293.15 298.15 1)

ρexp ± 2σ est

T K 293.15 298.15 298.15

Ref.

−3

kg ⋅ m

835.3 ± 2.0 768.9 ± 3.0 840.8 ± 2.0 836.8 ± 2.0

19-eyk1) 19-eyk1) 33-whi/woo1) 33-whi/woo1)

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

844.2 ± 2.0 835.0 ± 0.7 835.0 ± 0.7

61-mes/erz1) 88-cac/cos Recommended

Not included in calculation of recommended value.

4,4-Diethyl-2,2,3-trimethyl-3-hexanol

[500045-00-1]

C13H28O

MW = 200.36

411

C13H28O

MW = 200.36

412

Table 1. Experimental value with uncertainty. T K 283.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

906.0 ± 2.0

37-naz

2,2-Dimethyl-3-(1,1-dimethylethyl)3-heptanol

[42930-67-6]

Table 1. Experimental and recommended values with uncertainties. T K 293.15 293.15 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

860.6 ± 1.0 859.6 ± 1.0 860.1 ± 1.1

Landolt-Börnstein New Series IV/8G

54-mos/cox 60-pet/sok Recommended

236

2.1.8 Alkanols, C13 - C22

5,5-Dimethyl-2-neopentyl-1-hexanol

[109509-73-1]

C13H28O

MW = 200.36

413

C13H28O

MW = 200.36

414

C13H28O

MW = 200.36

415

C13H28O

MW = 200.36

416

C13H28O

MW = 200.36

417

C13H28O

MW = 200.36

418

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

847.0 ± 2.0

56-gol/kon

2,8-Dimethyl-5-ethyl-5-nonanol

[500001-93-4]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

867.7 ± 2.0

14-hal

3,3-Dimethyl-5-ethyl-4-nonanol

[500000-49-7]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

851.2 ± 1.0

41-whi/whi

2,4-Dimethyl-4-undecanol

[500045-01-2]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

825.2 ± 1.5

59-pet/zak

3,5-Dimethyl-5-undecanol

[107618-96-2]

Table 1. Experimental value with uncertainty. T K

301.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

827.2 ± 1.0

60-tha/vas

3-(1,1-Dimethylethyl)-2,2,5-trimethyl3-hexanol

[32579-70-7]

Table 1. Experimental and recommended values with uncertainties. T K

293.15 293.15 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

866.8 ± 1.0 867.6 ± 1.0 867.2 ± 1.0

54-mos/cox 60-pet/sok Recommended

Landolt-Börnstein New Series IV/8G

2.1.8 Alkanols, C13 - C22 2-Ethyl-1-undecanol

[54381-03-2]

237

C13H28O

MW = 200.36

419

C13H28O

MW = 200.36

420

C13H28O

MW = 200.36

421

C13H28O

MW = 200.36

422

C13H28O

MW = 200.36

423

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 47-sto 840.4 ± 2.0 6-Ethyl-6-undecanol

[5340-50-1]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 33-whi/wil 834.8 ± 2.0 4-Ethyl-3,3,5,5-tetramethyl-4-heptanol

[900002-19-9]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 54-mos/cox 892.8 ± 1.0 2-Methyl-1-dodecanol

[22663-61-2]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 298.15 29-lev/mik 844.0 ± 2.0 6-Methyl-6-dodecanol

[62958-40-1]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 3.0037 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.5019 · 10−1 (combined temperature ranges, unweighted). T = 273.15 to 338.15 K ρ = A + BT + CT 2 + DT 3 + … 9.86877 · 102 −3.15853 · 10−1 −7.40820 · 10−4

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

ρexp ± 2σ est −3

kg ⋅ m

273.15 845.20 ± 1.00 298.15 827.40 ± 1.00 308.15 819.00 ± 1.00

ρexp − ρcalc −3

kg ⋅ m

−0.13 0.55 −0.20

Ref. (Symbol in Fig. 1)

T K

ρexp ± 2σ est −3

kg ⋅ m

39-owe/qua( ) 318.15 811.00 ± 1.00 39-owe/qua( ) 328.15 803.50 ± 1.00 39-owe/qua( ) 338.15 795.50 ± 1.00

ρexp − ρcalc −3

kg ⋅ m

−0.40 0.04 0.14

Ref. (Symbol in Fig. 1)

39-owe/qua( ) 39-owe/qua( ) 39-owe/qua( ) cont.

Landolt-Börnstein New Series IV/8G

238

2.1.8 Alkanols, C13 - C22

ρ

ρ

6-Methyl-6-dodecanol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15

ρ ± σ fit kg ⋅ m−3

ρ ± σ fit kg ⋅ m−3

T K

847.59 ± 1.69 840.36 ± 1.36 832.98 ± 1.17 830.62 ± 1.12

826.85 ± 1.06 825.45 ± 1.04 817.77 ± 0.95 809.94 ± 0.93

298.15 300.00 310.00 320.00

4-(1-Methylethyl)-3,3,6-trimethyl4-heptanol

[900002-20-2]

T K

330.00 340.00 350.00

C13H28O

ρ ± σ fit kg ⋅ m−3 801.97 ± 1.14 793.85 ± 1.71 785.58 ± 2.66

MW = 200.36

424

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

864.8 ± 1.0

54-mos/cox

Landolt-Börnstein New Series IV/8G

2.1.8 Alkanols, C13 - C22 5-(2-Methylpropyl)-5-nonanol

[500013-26-3]

239

C13H28O

MW = 200.36

425

C13H28O

MW = 200.36

426

C13H28O

MW = 200.36

427

C13H28O

MW = 200.36

428

C13H28O

MW = 200.36

429

Table 1. Experimental value with uncertainty. T K 288.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

843.8 ± 1.5

37-pet/mal

2,2,3,3,4-Pentamethyl-4-octanol

[100799-11-9]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

876.3 ± 2.0

60-pet/kao

5-Propyl-5-decanol

[62958-41-2]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

298.15

Ref.

kg ⋅ m−3

832.0 ± 2.0

44-qua/sma

4-Propyl-3,3,6-trimethyl-4-heptanol

[900002-21-3]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

859.8 ± 1.0

54-mos/cox

1-Tridecanol

[112-70-9]

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 0.476. Coefficient ρ = A + BT 1022.21 A B −0.640 Table 2. Experimental values with uncertainties and deviation from calculated values. T K 323.15 313.15 333.15

ρexp ± 2σ est −3

kg ⋅ m

816.5 ± 1.0 821.5 ± 0.6 808.9 ± 0.6

ρexp − ρcalc

Ref.

−3

kg ⋅ m

1.10 −0.30 −0.10

63-vil/gav 77-bel/bub 77-bel/bub cont.

Landolt-Börnstein New Series IV/8G

240

2.1.8 Alkanols, C13 - C22

1-Tridecanol (cont.) Table 3. Recommended values. ρexp ± 2σ est

T K

kg ⋅ m

823.8 ± 1.0 817.4 ± 0.8

310.00 320.00

ρexp ± 2σ est

T K

−3

kg ⋅ m−3

811.0 ± 0.9 804.6 ± 1.2

330.00 340.00

2-Tridecanol

[1653-31-2]

C13H28O

MW = 200.36

430

Table 1. Fit with estimated B coefficient for 4 accepted points. Deviation σw = 0.944. Coefficient ρ = A + BT 1035.14 A B −0.700 Table 2. Experimental values with uncertainties and deviation from calculated values. T K 307.25 320.45 333.75 287.65

ρexp ± 2σ est −3

kg ⋅ m

821.5 ± 2.0 810.9 ± 2.0 801.2 ± 2.0 832.6 ± 2.0

ρexp − ρcalc

Ref.

−3

kg ⋅ m

1.43 0.07 −0.32 −1.19

11-pic/ken 11-pic/ken 11-pic/ken 12-pic/ken

Table 3. Recommended values. T K 280.00 290.00 293.15

ρexp ± 2σ est

ρexp ± 2σ est

T K 298.15 310.00 320.00

kg ⋅ m−3

839.1 ± 3.8 832.1 ± 3.0 829.9 ± 2.8

3-Tridecanol

kg ⋅ m−3

826.4 ± 2.5 818.1 ± 2.0 811.1 ± 2.2

[10289-68-6]

T K 330.00 340.00

ρexp ± 2σ est kg ⋅ m−3

804.1 ± 2.7 797.1 ± 3.4

C13H28O

MW = 200.36

431

C13H28O

MW = 200.36

432

Table 1. Experimental value with uncertainty. T K 353.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

786.5 ± 3.0

13-pic/ken

4-Tridecanol

[26215-92-9]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

823.4 ± 2.0

48-pet/old

Landolt-Börnstein New Series IV/8G

2.1.8 Alkanols, C13 - C22 2,2,3-Trimethyl-4-propyl-3-heptanol

[500002-64-2]

241

C13H28O

MW = 200.36

433

C13H28O

MW = 200.36

434

C13H28O

MW = 200.36

435

C14H30O

MW = 214.39

436

Table 1. Experimental value with uncertainty. T K 285.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

859.0 ± 2.0

37-naz

2,3,6-Trimethyl-1-decanol

[500002-12-0]

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

835.1 ± 2.0

38-wer/bog

2,5,9-Trimethyl-5-decanol

[500001-91-2]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

284.15

Ref.

kg ⋅ m−3

844.4 ± 2.0

28-esc

5-Butyl-5-decanol

[5340-34-1]

Table 1. Fit with estimated B coefficient for 4 accepted points. Deviation σw = 0.926. Coefficient ρ = A + BT 1048.44 A B −0.720 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

298.15 298.15 318.15 328.15 293.15 1)

−3

kg ⋅ m

834.5 ± 2.0 834.8 ± 2.0 818.9 ± 2.0 810.9 ± 2.0 845.4 ± 6.0

ρexp − ρcalc

Ref.

−3

kg ⋅ m

0.73 1.03 −0.47 −1.27 8.03

33-whi/wil 44-qua/sma 44-qua/sma 44-qua/sma 61-mes/erz1)

Not included in calculation of linear coefficients.

Table 3. Recommended values. T K 290.00 293.15

Landolt-Börnstein New Series IV/8G

ρexp ± 2σ est kg ⋅ m−3

839.6 ± 2.7 837.4 ± 2.4

T K 298.15 310.00

ρexp ± 2σ est kg ⋅ m−3

833.8 ± 2.1 825.2 ± 1.7

T K 320.00 330.00

ρexp ± 2σ est kg ⋅ m−3

818.0 ± 1.9 810.8 ± 2.6

242 2,2-Dimethyl-3-(1,1-dimethylethyl)3-octanol

2.1.8 Alkanols, C13 - C22 [500045-08-9]

C14H30O

MW = 214.39

437

C14H30O

MW = 214.39

438

C14H30O

MW = 214.39

439

C14H30O

MW = 214.39

440

C14H30O

MW = 214.39

441

C14H30O

MW = 214.39

442

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 60-pet/sok 861.4 ± 1.5 3,3-Dimethyl-4-(1,1-dimethylethyl)4-octanol

[900002-34-8]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 54-mos/cox 873.4 ± 1.0 2,2-Dimethyl-1-dodecanol

[92318-63-3]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 64-blo/hag 836.3 ± 2.0 3,3-Dimethyl-4-(2-methylpropyl)4-octanol

[900002-22-4]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 54-mos/cox 856.8 ± 1.0 4-(1,1-Dimethylethyl)-3,3,6-trimethyl4-heptanol

[900002-25-7]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 54-mos/cox 879.4 ± 1.0 5-(2,2-Dimethylpropyl)-5-nonanol

[5340-38-5]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 38-whi/pop-11) 832.0 ± 3.0 293.15 42-whi/for 840.3 ± 2.0 293.15 Recommended 840.3 ± 2.0 1)

Not included in calculation of recommended value.

Landolt-Börnstein New Series IV/8G

2.1.8 Alkanols, C13 - C22 7-Ethyl-2-methyl-4-undecanol

243

[103-20-8]

C14H30O

MW = 214.39

443

[57233-27-9]

C14H30O

MW = 214.39

444

[32836-44-5]

C14H30O

MW = 214.39

445

[98930-89-3]

C14H30O

MW = 214.39

446

[116436-16-9]

C14H30O

MW = 214.39

447

[20194-46-1]

C14H30O

MW = 214.39

448

C14H30O

MW = 214.39

449

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 20.00 58-ano-5 834.1 ± 1.0

2-Methyl-3-(1-methylethyl)-3-decanol Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15

856.2 ± 2.0

62-pet/kap

2-Methyl-2-tridecanol

Table 1. Experimental values with uncertainties. ρexp ± 2σ est T Ref. K kg ⋅ m−3 289.75 19-eyk 832.0 ± 2.0 354.95 19-eyk 784.1 ± 4.0

2-Methyl-3-tridecanol Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 12-pic/ken 839.0 ± 2.0

4-Methyl-4-tridecanol Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 297.15 19-eyk 829.2 ± 2.0

11-Methyl-1-tridecanol

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 298.15 62-lar/sal 834.4 ± 1.0 L(+)-11-Methyl-1-tridecanol Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3

298.15

834.4 ± 0.6

Landolt-Börnstein New Series IV/8G

62-lar/sal

[500006-93-9]

244

2.1.8 Alkanols, C13 - C22

6-(1-Methylethyl)-6-undecanol

[500002-69-7]

C14H30O

MW = 214.39

450

C14H30O

MW = 214.39

451

C14H30O

MW = 214.39

452

C14H30O

MW = 214.39

453

C14H30O

MW = 214.39

454

C14H30O

MW = 214.39

455

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

842.5 ± 1.0

46-hus/bai

4-(2-Methylpropyl)-2,2,6-trimethyl4-heptanol

[500002-08-4]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

831.7 ± 2.0

42-whi/for

4-(2-Methylpropyl)-3,3,6-trimethyl4-heptanol

[900002-24-6]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

853.0 ± 1.0

54-mos/cox

2,2,3,3,4-Pentamethyl-4-nonanol

[108272-61-3]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

875.1 ± 2.0

60-pet/kao

4,4,5,6,6-Pentamethyl-5-nonanol

[500002-06-2]

Table 1. Experimental value with uncertainty. T K

288.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

887.6 ± 2.0

2-Pentyl-1-nonanol

37-naz [5333-48-2]

Table 1. Experimental values with uncertainties. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 288.15 01-gue 840.5 ± 2.0 297.15 38-mas 837.7 ± 2.0

Landolt-Börnstein New Series IV/8G

2.1.8 Alkanols, C13 - C22 4-Propyl-3,3,5,5-tetramethyl-4-heptanol

245

[900002-88-2]

C14H30O

MW = 214.39

456

[500002-03-9]

C14H30O

MW = 214.39

457

[112-72-1]

C 14H30O

MW = 214.39

458

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 54-mos/cox 888.2 ± 1.0

6-Propyl-6-undecanol Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 298.15 33-whi/wil 833.6 ± 2.0

1-Tetradecanol

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 8.9110 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.2677 · 10−1 (combined temperature ranges, unweighted).

Coefficient A B C D

T = 293.15 to 573.15 K ρ = A + BT + CT 2 + DT 3 + … 1.01416 · 103 −5.58592 · 10−1 −1.11840 · 10−4 −2.07120 · 10−7

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 311.15 311.15 323.15 323.15 372.05 372.05 311.55 313.15 333.15 353.15 293.15 313.15 333.15 353.15 373.15 393.15 413.15 1)

823.60 ± 2.00 823.60 ± 1.00 815.30 ± 1.00 815.30 ± 2.00 781.30 ± 1.00 781.30 ± 2.00 824.00 ± 2.00 822.00 ± 2.00 807.00 ± 2.00 794.00 ± 2.00 834.00 ± 2.00 822.70 ± 1.00 807.90 ± 1.00 793.10 ± 1.00 778.40 ± 1.00 766.60 ± 1.00 748.80 ± 1.00

0.31 0.31 0.31 0.31 1.11 1.11 0.99 0.09 −1.00 0.17 −1.58 0.79 −0.10 −0.73 −0.99 1.92 −0.88

1883-kra( ) 1883-kra( ) 1883-kra( ) 1883-kra1) 1883-kra( ) 1883-kra( ) 49-tsv/mar(◆) 56-rat/cur(∆) 56-rat/cur1) 56-rat/cur1) 58-ano-3(∇) 58-cos/bow( ) 58-cos/bow( ) 58-cos/bow( ) 58-cos/bow( ) 58-cos/bow1) 58-cos/bow( )

433.15 453.15 473.15 493.15 513.15 533.15 553.15 573.15 318.15 323.15 328.15 333.15 338.15 343.15 348.15 353.15

734.00 ± 1.00 718.80 ± 1.00 703.20 ± 1.00 686.50 ± 1.00 670.00 ± 1.00 653.40 ± 1.00 636.20 ± 1.00 617.80 ± 1.00 817.60 ± 0.60 814.60 ± 0.60 811.60 ± 0.60 808.70 ± 0.60 804.00 ± 0.60 801.10 ± 0.60 798.10 ± 0.60 793.40 ± 0.60

−0.39 0.00 0.31 −0.15 −0.08 0.23 0.30 −0.47 −0.86 −0.39 0.10 0.70 −0.48 0.16 0.71 −0.43

Ref. (Symbol in Fig. 1)

58-cos/bow( ) 58-cos/bow( ) 58-cos/bow( ) 58-cos/bow( ) 58-cos/bow( ) 58-cos/bow( ) 58-cos/bow( ) 58-cos/bow( ) 92-lie/sen-1(✕ ) 92-lie/sen-1(✕ ) 92-lie/sen-1(✕ ) 92-lie/sen-1(✕ ) 92-lie/sen-1(✕ ) 92-lie/sen-1(✕ ) 92-lie/sen-1(✕ ) 92-lie/sen-1(✕ )

Not included in Fig. 1.

Further references: [60-pet/kao, 60-pet/sok, 63-vil/gav]. Landolt-Börnstein New Series IV/8G

cont.

246

2.1.8 Alkanols, C13 - C22

ρ

ρ

1-Tetradecanol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

290.00 293.15 298.15 300.00 310.00 320.00 330.00 340.00 350.00 360.00 370.00

ρ ± σ fit kg ⋅ m−3 837.71 ± 2.11 835.58 ± 2.00 832.19 ± 1.84 830.93 ± 1.79 824.08 ± 1.52 817.17 ± 1.29 810.20 ± 1.12 803.17 ± 0.99 796.07 ± 0.89 788.91 ± 0.82 781.68 ± 0.77

T K

380.00 390.00 400.00 410.00 420.00 430.00 440.00 450.00 460.00 470.00 480.00

ρ ± σ fit kg ⋅ m−3 774.38 ± 0.74 767.01 ± 0.73 759.58 ± 0.73 752.06 ± 0.74 744.48 ± 0.77 736.82 ± 0.80 729.09 ± 0.85 721.27 ± 0.91 713.38 ± 0.97 705.42 ± 1.03 697.36 ± 1.10

T K

490.00 500.00 510.00 520.00 530.00 540.00 550.00 560.00 570.00 580.00

ρ ± σ fit kg ⋅ m−3 689.23 ± 1.16 681.02 ± 1.22 672.72 ± 1.28 664.33 ± 1.33 655.86 ± 1.37 647.30 ± 1.41 638.65 ± 1.45 629.90 ± 1.50 621.07 ± 1.57 612.14 ± 1.66

Landolt-Börnstein New Series IV/8G

2.1.8 Alkanols, C13 - C22 3-Tetradecanol

[1653-32-3]

247

C14H30O

MW = 214.39

459

C14H30O

MW = 214.39

460

C 15H32O

MW = 228.42

461

C15H32O

MW = 228.42

462

C15H32O

MW = 228.42

463

C15H32O

MW = 228.42

464

Table 1. Experimental value with uncertainty. T K 353.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

788.5 ± 2.0

13-pic/ken

4-Tetradecanol

[1653-33-4]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

305.15

Ref.

kg ⋅ m−3

823.1 ± 3.0

48-pet/old

4-Butyl-3,3,5,5-tetramethyl-4-heptanol

[900002-89-3]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

kg ⋅ m−3

884.9 ± 1.0

54-mos/cox

6-Butyl-6-undecanol

[5396-08-7]

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

834.4 ± 2.0

33-whi/wil

2,2-Dimethyl-3-(1,1-dimethylethyl)3-nonanol

[101082-11-5]

Table 1. Experimental values with uncertainties. T K 293.15 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

860.3 ± 2.0 860.3 ± 2.0

57-pet/sok 60-pet/sok

2,8-Dimethyl-5-(2-methylpropyl)5-nonanol

[500002-16-4]

Table 1. Fit with estimated B coefficient for 4 accepted points. Deviation σw = 0.060. Coefficient ρ = A + BT 1068.38 A B −0.800 cont.

Landolt-Börnstein New Series IV/8G

248

2.1.8 Alkanols, C13 - C22

2,8-Dimethyl-5-(2-methylpropyl)-5-nonanol (cont.) Table 2. Experimental values with uncertainties and deviation from calculated values. T K

273.15 283.55 273.15 283.55

ρexp ± 2σ est

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−3

kg ⋅ m

849.8 ± 2.0 841.6 ± 2.0 849.8 ± 2.0 841.6 ± 2.0

−0.06 0.06 −0.06 0.06

04-gri 04-gri 04-gri-1 04-gri-1

Table 3. Recommended values. T K

270.00 280.00 290.00

ρexp ± 2σ est kg ⋅ m−3

852.4 ± 1.8 844.4 ± 1.8 836.4 ± 1.9

6,10-Dimethyl-2-tridecanol

[101082-12-6]

C15H32O

MW = 228.42

465

C15H32O

MW = 228.42

466

C15H32O

MW = 228.42

467

Table 1. Experimental and recommended values with uncertainties. T K 293.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

830.3 ± 1.0 888.2 ± 2.0 830.3 ± 1.0

49-naz/zar-1 61-shv/pet1) Recommended

Not included in calculation of recommended value.

2-Methyl-2-tetradecanol

[27570-83-8]

Table 1. Experimental and recommended values with uncertainties. T K 293.15 293.15 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

836.0 ± 2.0 838.0 ± 2.0 837.0 ± 2.1

42-pet/che 57-for/lan Recommended

6-(2-Methylpropyl)-6-undecanol

[500002-70-0]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

836.7 ± 2.0

46-hus/bai Landolt-Börnstein New Series IV/8G

2.1.8 Alkanols, C13 - C22 1-Pentadecanol

[629-76-5]

249

C15H32O

MW = 228.42

468

C15H32O

MW = 228.42

469

C15H32O

MW = 228.42

470

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.350. Coefficient ρ = A + BT 1025.57 A B −0.640

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 295.55 323.15 313.15 333.15 1)

ρexp ± 2σ est −3

kg ⋅ m

836.4 ± 2.0 819.2 ± 2.0 824.8 ± 0.6 812.7 ± 0.6

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−0.01 0.45 −0.35 0.35

47-sto1) 63-vil/gav1) 77-bel/bub 77-bel/bub

Not included in calculation of linear coefficients.

Table 3. Recommended values. ρexp ± 2σ est

T K 310.00 320.00 330.00 340.00

kg ⋅ m−3

827.2 ± 0.8 820.8 ± 0.5 814.4 ± 0.6 808.0 ± 1.0

3-Pentadecanol

[53346-71-7]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

353.15

Ref.

kg ⋅ m−3

792.1 ± 3.0

13-pic/ken

3,7,11-Trimethyl-3-dodecanol

[7278-65-1]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

−3

kg ⋅ m

838.7 ± 2.0

Landolt-Börnstein New Series IV/8G

58-naz/gus

250

2.1.8 Alkanols, C13 - C22

2-Butyl-1-dodecanol

[21078-85-3]

C16H34O

MW = 242.45

471

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 7.9175 · 10−1 (combined temperature ranges, weighted), σc,uw = 5.0211 · 10−1 (combined temperature ranges, unweighted). Coefficient A B

T = 293.15 to 373.15 K ρ = A + BT + CT 2 + DT 3 + … 1.03807 · 103 −6.84381 · 10−1

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

Ref. (Symbol in Fig. 1)

0.49 0.86 0.78 0.37

33-bin/ste(✕ ) 33-bin/ste(✕ ) 33-bin/ste(✕ ) 33-bin/ste(✕ )

837.94 ± 1.00 831.46 ± 1.00 824.54 ± 1.00 810.44 ± 1.00

T K

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

353.15 796.81 ± 1.00 373.15 782.72 ± 1.00 293.15 834.50 ± 2.00

0.43 0.02 −2.95

Ref. (Symbol in Fig. 1) 33-bin/ste(✕ ) 33-bin/ste(✕ ) 35-cox/rei( )

ρ

ρ

293.15 303.15 313.15 333.15

ρexp ± 2σ est

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont. Landolt-Börnstein New Series IV/8G

2.1.8 Alkanols, C13 - C22

251

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ).

ρ ± σ fit kg ⋅ m−3

T K

T K

839.60 ± 1.79 837.45 ± 1.64 834.03 ± 1.44 832.76 ± 1.37

290.00 293.15 298.15 300.00

310.00 320.00 330.00 340.00

5-Butyl-5-dodecanol

ρ ± σ fit kg ⋅ m−3

T K

825.92 ± 1.05 819.07 ± 0.84 812.23 ± 0.75 805.38 ± 0.78

350.00 360.00 370.00 380.00

ρ ± σ fit kg ⋅ m−3 798.54 ± 0.93 791.70 ± 1.18 784.85 ± 1.51 778.01 ± 1.94

[93314-38-6]

C16H34O

MW = 242.45

472

[93314-37-5]

C16H34O

MW = 242.45

473

[5286-18-0]

C16H34O

MW = 242.45

474

[500000-42-0]

C 16H34O

MW = 242.45

475

[25354-99-8]

C16H34O

MW = 242.45

476

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 37-pet/and 841.5 ± 1.0

2,2-Dimethyl-3-(1,1-dimethylethyl)3-decanol Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15

865.6 ± 2.0

62-pet/kap

2,2-Dimethyl-1-tetradecanol Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 64-blo/hag 840.0 ± 2.0

2,2-Dimethyl-3-tetradecanol Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15

835.6 ± 1.0

2-Ethyl-1-tetradecanol

41-whi/whi

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 8.6253 · 10-1 (combined temperature ranges, weighted), σc,uw = 5.4877 · 10-1 (combined temperature ranges, unweighted). Coefficient A B

T = 293.15 to 373.15 K ρ = A + BT + CT 2 + DT 3 + … 1.04120 · 103 −6.86917 · 10−1

cont. Landolt-Börnstein New Series IV/8G

252

2.1.8 Alkanols, C13 - C22

2-Ethyl-1-tetradecanol (cont.) Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

kg ⋅ m

Ref. (Symbol in Fig. 1)

840.48 ± 1.00 833.61 ± 1.00 826.99 ± 1.00 813.01 ± 1.00

0.65 0.65 0.90 0.66

33-bin/ste(✕ ) 33-bin/ste(✕ ) 33-bin/ste(✕ ) 33-bin/ste(✕ )

kg ⋅ m

−3

T K

ρexp ± 2σ est

ρexp − ρcalc kg ⋅ m

Ref. (Symbol in Fig. 1)

0.37 −0.00 −3.23

33-bin/ste(✕ ) 33-bin/ste(✕ ) 35-cox/rei( )

−3

−3

kg ⋅ m

353.15 798.98 ± 1.00 373.15 784.87 ± 1.00 293.15 836.60 ± 2.00

ρ

ρ

293.15 303.15 313.15 333.15

ρexp − ρcalc

−3

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

290.00 293.15 298.15 300.00

ρ ± σ fit kg ⋅ m−3 841.99 ± 1.79 839.83 ± 1.64 836.39 ± 1.44 835.12 ± 1.37

T K

310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 828.25 ± 1.05 821.38 ± 0.84 814.51 ± 0.75 807.65 ± 0.78

T K

350.00 360.00 370.00 380.00

ρ ± σ fit kg ⋅ m−3 800.78 ± 0.93 793.91 ± 1.18 787.04 ± 1.51 780.17 ± 1.94

Landolt-Börnstein New Series IV/8G

2.1.8 Alkanols, C13 - C22 3-Ethyl-3-tetradecanol

[101433-18-5]

253

C16H34O

MW = 242.45

477

C16H34O

MW = 242.45

478

Table 1. Experimental value with uncertainty. T K 288.45

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

846.0 ± 3.0

19-eyk

2-Heptyl-1-nonanol

[25355-03-7]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 1.3014 · 10−1 (combined temperature ranges, weighted), σc,uw = 6.5072 · 10−2 (combined temperature ranges, unweighted). T = 293.15 to 373.15 K ρ = A + BT + CT 2 + DT 3 + … 1.00360 · 103 −4.62418 · 10−1 −3.53389 · 10−4

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

293.15 837.59 ± 1.00 303.15 830.91 ± 1.00 313.15 824.40 ± 1.00

−0.09 −0.04 0.26

Ref. (Symbol in Fig. 1)

33-bin/ste( ) 33-bin/ste( ) 33-bin/ste( )

T K

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

333.15 810.24 ± 1.00 353.15 796.11 ± 1.00 373.15 781.92 ± 1.00

−0.09 −0.12 0.07

Ref. (Symbol in Fig. 1)

33-bin/ste( ) 33-bin/ste( ) 33-bin/ste( )

Further references: [35-cox/rei].

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

290.00 293.15 298.15 300.00

ρ ± σ fit kg ⋅ m−3 839.78 ± 1.54 837.68 ± 1.42 834.32 ± 1.27 833.07 ± 1.22

T K

310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 826.29 ± 1.06 819.44 ± 1.00 812.52 ± 0.98 805.53 ± 0.96

T K

350.00 360.00 370.00 380.00

ρ ± σ fit kg ⋅ m−3 798.47 ± 0.98 791.33 ± 1.13 784.13 ± 1.50 776.86 ± 2.13

cont.

Landolt-Börnstein New Series IV/8G

254

2.1.8 Alkanols, C13 - C22

ρ

ρ

2-Heptyl-1-nonanol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

1-Hexadecanol

[36653-82-4]

C16H34O

MW = 242.45

479

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 2.9130 · 10−1 (combined temperature ranges, weighted), σc,uw = 5.8696 · 10−2 (combined temperature ranges, unweighted). Coefficient A B C D

T = 321.15 to 573.15 K ρ = A + BT + CT 2 + DT 3 + … 9.25311 · 102 1.01083 · 10−1 −1.68710 · 10−3 1.06172 · 10−6

cont.

Landolt-Börnstein New Series IV/8G

2.1.8 Alkanols, C13 - C22

255

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

ρexp ± 2σ est −3

kg ⋅ m

crystal 78.15 1000.0 ± 3.0 194.15 974.0 ± 3.0 liquid 322.65 817.60 ± 1.00 322.65 817.60 ± 1.00 333.15 810.50 ± 1.00 333.15 810.50 ± 1.00 371.85 783.70 ± 1.00 371.85 783.70 ± 1.00 298.15 888.60 ± 0.60 323.15 817.60 ± 0.60 321.15 819.00 ± 1.00 323.15 817.60 ± 1.00 333.15 810.50 ± 1.00 353.15 797.10 ± 1.00 373.15 783.00 ± 1.00 393.15 768.40 ± 1.00 413.15 753.70 ± 1.00 433.15 738.70 ± 1.00 453.15 723.30 ± 1.00 473.15 708.20 ± 1.00 493.15 692.80 ± 1.00 1)

ρexp − ρcalc −3

kg ⋅ m

Ref. (Symbol in Fig. 1)

T K

513.15 533.15 553.15 573.15 1883-kra1) 323.08 1883-kra1) 333.09 1883-kra1) 333.14 1883-kra1) 333.15 1883-kra(◆) 342.95 1883-kra(◆) 343.26 38-bak/smy1) 352.77 38-bak/smy( ) 353.19 355.38 53-kre-1(∆) 53-kre-11) 361.46 58-cos/bow1) 361.61 58-cos/bow1) 367.39 58-cos/bow(∇) 370.40 58-cos/bow(∇) 333.15 58-cos/bow(∇) 338.15 58-cos/bow(∇) 343.15 58-cos/bow(∇) 348.15 58-cos/bow(∇) 353.15 58-cos/bow(∇) 30-bil/fis-1 30-bil/fis-1

−0.36 −0.36 −0.50 −0.50 −0.51 −0.51 54.98 −0.03 0.06 −0.03 −0.50 −0.26 −0.28 −0.40 −0.27 −0.15 −0.17 0.29 0.60

ρexp ± 2σ est

ρexp − ρcalc kg ⋅ m−3

−3

kg ⋅ m

677.00 ± 1.00 660.70 ± 1.00 645.40 ± 1.00 628.80 ± 1.00 817.80 ± 0.20 811.04 ± 0.20 810.98 ± 0.20 810.92 ± 0.20 804.23 ± 0.20 804.30 ± 0.20 797.69 ± 0.20 797.42 ± 0.20 795.85 ± 0.20 791.54 ± 0.20 791.53 ± 0.20 787.42 ± 0.20 785.34 ± 0.20 811.30 ± 0.60 806.80 ± 0.60 803.90 ± 0.60 800.90 ± 0.60 797.80 ± 0.60

0.61 0.15 0.69 −0.13 0.13 0.00 −0.02 −0.08 −0.15 0.14 0.06 0.08 0.04 −0.02 0.07 0.04 0.10 0.30 −0.83 −0.34 0.08 0.44

Ref. (Symbol in Fig. 1) 58-cos/bow(∇) 58-cos/bow(∇) 58-cos/bow(∇) 58-cos/bow(∇) 73-fin(✕ ) 73-fin(✕ ) 73-fin(✕ ) 73-fin(✕ ) 73-fin(✕ ) 73-fin(✕ ) 73-fin(✕ ) 73-fin(✕ ) 73-fin(✕ ) 73-fin(✕ ) 73-fin(✕ ) 73-fin(✕ ) 73-fin(✕ ) 92-lie/sen-1( ) 92-lie/sen-1( ) 92-lie/sen-1( ) 92-lie/sen-1( ) 92-lie/sen-1( )

Not included in Fig. 1.

Further references: [1893-eyk, 22-tro, 31-del, 49-hos/ste, 50-boe/ned, 56-rat/cur, 63-vil/gav, 69-kat/pat].

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

320.00 330.00 340.00 350.00 360.00 370.00 380.00 390.00 400.00

ρ ± σ fit kg ⋅ m−3 819.69 ± 0.41 813.10 ± 0.43 806.38 ± 0.46 799.54 ± 0.50 792.59 ± 0.54 785.53 ± 0.58 778.36 ± 0.62 771.11 ± 0.67 763.76 ± 0.71

T K

410.00 420.00 430.00 440.00 450.00 460.00 470.00 480.00 490.00

ρ ± σ fit kg ⋅ m−3 756.33 ± 0.75 748.82 ± 0.79 741.25 ± 0.84 733.61 ± 0.88 725.91 ± 0.93 718.16 ± 0.97 710.37 ± 1.01 702.54 ± 1.05 694.68 ± 1.08

T K

500.00 510.00 520.00 530.00 540.00 550.00 560.00 570.00 580.00

ρ ± σ fit kg ⋅ m−3 686.79 ± 1.11 678.89 ± 1.15 670.97 ± 1.18 663.04 ± 1.22 655.12 ± 1.27 647.20 ± 1.33 639.30 ± 1.42 631.41 ± 1.53 623.55 ± 1.68 cont.

Landolt-Börnstein New Series IV/8G

256

2.1.8 Alkanols, C13 - C22

ρ

ρ

1-Hexadecanol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

3-Hexadecanol

[593-03-3]

C16H34O

MW = 242.45

480

C16H34O

MW = 242.45

481

Table 1. Experimental value with uncertainty. T K

353.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

790.7 ± 2.0

2-Hexyl-1-decanol

13-pic/ken

[2425-77-6]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 1.1013 (combined temperature ranges, weighted), σc,uw = 5.0818 · 10−1 (combined temperature ranges, unweighted). Coefficient A B

T = 289.65 to 373.15 K ρ = A + BT + CT 2 + DT 3 + … 1.03893 · 103 −6.88973 · 10−1 cont.

Landolt-Börnstein New Series IV/8G

2.1.8 Alkanols, C13 - C22

257

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

kg ⋅ m

Ref. (Symbol in Fig. 1)

837.24 ± 1.00 830.56 ± 1.00 823.79 ± 1.00 809.78 ± 1.00

0.28 0.49 0.61 0.38

33-bin/ste(✕ ) 33-bin/ste(✕ ) 33-bin/ste(✕ ) 33-bin/ste(✕ )

kg ⋅ m

−3

T K

353.15 373.15 293.15 289.65

ρexp ± 2σ est

ρexp − ρcalc kg ⋅ m−3

−3

kg ⋅ m

795.67 ± 1.00 781.86 ± 1.00 833.60 ± 2.00 840.90 ± 2.00

0.05 0.02 −3.36 1.53

Ref. (Symbol in Fig. 1) 33-bin/ste(✕ ) 33-bin/ste(✕ ) 35-cox/rei( ) 38-mas( )

ρ

ρ

293.15 303.15 313.15 333.15

ρexp − ρcalc

−3

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

280.00 290.00 293.15 298.15 300.00

Landolt-Börnstein New Series IV/8G

ρ ± σ fit kg ⋅ m−3 846.02 ± 2.28 839.13 ± 1.77 836.96 ± 1.63 833.51 ± 1.43 832.24 ± 1.36

T K

310.00 320.00 330.00 340.00 350.00

ρ ± σ fit kg ⋅ m−3 825.35 ± 1.06 818.46 ± 0.86 811.57 ± 0.78 804.68 ± 0.81 797.79 ± 0.96

T K

360.00 370.00 380.00

ρ ± σ fit kg ⋅ m−3 790.90 ± 1.20 784.01 ± 1.52 777.12 ± 1.94

258

2.1.8 Alkanols, C13 - C22

2-Methyl-1-pentadecanol

[25354-98-7]

C16H34O

MW = 242.45

482

C16H34O

MW = 242.45

483

C16H34O

MW = 242.45

484

C16H34O

MW = 242.45

485

C16H34O

MW = 242.45

486

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 35-cox/rei 832.0 ± 1.0 2-Methyl-2-pentadecanol

[60129-23-9]

Table 1. Experimental values with uncertainties. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.35 19-eyk 826.5 ± 2.0 353.95 19-eyk 764.0 ± 2.0 6-Methyl-6-pentadecanol

[108836-86-8]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 30-dav/dix 831.6 ± 2.0 9-Methyl-7-pentadecanol

[500002-20-0]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 288.15 12-gue 835.1 ± 2.0 2-Pentyl-1-undecanol

[25355-02-6]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 7.9132 · 10−1 (combined temperature ranges, weighted), σc,uw = 4.9799 · 10−1 (combined temperature ranges, unweighted). Coefficient A B

T = 293.15 to 373.15 K ρ = A + BT + CT 2 + DT 3 + … 1.03716 · 103 −6.82767 · 10−1

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc Ref. (Symbol ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 293.15 838.08 ± 1.00 1.07 33-bin/ste(✕ ) 353.15 796.56 ± 1.00 0.52 33-bin/ste(✕ ) 303.15 830.70 ± 1.00 0.52 33-bin/ste(✕ ) 373.15 782.47 ± 1.00 0.08 33-bin/ste(✕ ) 313.15 823.66 ± 1.00 0.31 33-bin/ste(✕ ) 293.15 834.10 ± 2.00 −2.91 35-cox/rei( ) 333.15 810.11 ± 1.00 0.41 33-bin/ste(✕ ) cont.

Landolt-Börnstein New Series IV/8G

259

ρ

ρ

2.1.8 Alkanols, C13 - C22

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ).

ρ ± σ fit kg ⋅ m−3

T K

839.16 ± 1.79 837.01 ± 1.64 833.59 ± 1.44 832.33 ± 1.37

290.00 293.15 298.15 300.00

ρ ± σ fit kg ⋅ m−3

T K

825.50 ± 1.05 818.68 ± 0.84 811.85 ± 0.75 805.02 ± 0.78

310.00 320.00 330.00 340.00

6-Pentyl-6-undecanol

[5331-63-5]

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

829.3 ± 2.0

Landolt-Börnstein New Series IV/8G

33 -whi/wil -0

T K

350.00 360.00 370.00 380.00

C16H34O

ρ ± σ fit kg ⋅ m−3 798.19 ± 0.93 791.37 ± 1.18 784.54 ± 1.51 777.71 ± 1.94

MW = 242.45

487

260

2.1.8 Alkanols, C13 - C22

2-Propyl-1-tridecanol

[25355-00-4]

C16H34O

MW = 242.45

488

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 2.6674 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.1929 · 10−1 (combined temperature ranges, unweighted). Coefficient A B

T = 293.15 to 373.15 K ρ = A + BT + CT 2 + DT 3 + … 1.04215 · 103 −6.93516 · 10−1

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

293.15 838.43 ± 1.00 303.15 832.09 ± 1.00 313.15 825.42 ± 1.00

−0.41 0.18 0.45

Ref. (Symbol in Fig. 1)

33-bin/ste( ) 33-bin/ste( ) 33-bin/ste( )

T K

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

333.15 810.96 ± 1.00 353.15 797.19 ± 1.00 373.15 783.33 ± 1.00

−0.14 −0.04 −0.03

Ref. (Symbol in Fig. 1)

33-bin/ste( ) 33-bin/ste( ) 33-bin/ste( )

ρ

ρ

Further references: [35-cox/rei].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont. Landolt-Börnstein New Series IV/8G

2.1.8 Alkanols, C13 - C22

261

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ).

ρ ± σ fit kg ⋅ m−3

T K

841.03 ± 1.37 838.84 ± 1.32 835.38 ± 1.24 834.09 ± 1.21

290.00 293.15 298.15 300.00

ρ ± σ fit kg ⋅ m−3

T K

827.16 ± 1.05 820.22 ± 0.90 813.29 ± 0.82 806.35 ± 0.82

310.00 320.00 330.00 340.00

5-Propyl-4-tridecanol

[500002-21-1]

T K

350.00 360.00 370.00 380.00

ρ ± σ fit kg ⋅ m−3 799.42 ± 0.92 792.48 ± 1.12 785.55 ± 1.45 778.61 ± 1.92

C16H34O

MW = 242.45

489

C 17H36O

MW = 256.47

490

C17H36O

MW = 256.47

491

C17H36O

MW = 256.47

492

C17H36O

MW = 256.47

493

Table 1. Experimental value with uncertainty. T K 288.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

831.0 ± 2.0

48-pet/old

3,9-Diethyl-6-tridecanol

[123-24-0]

Table 1. Experimental values with uncertainties. ρexp ± 2σ est

T K

293.15 293.15

Ref.

−3

kg ⋅ m

846.0 ± 1.0 846.1 ± 1.0

53-ano-15 58-ano-5

1-Heptadecanol

[1454-85-9]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

323.15

Ref.

kg ⋅ m−3

815.3 ± 2.0

63-vil/gav

2-Heptadecanol

[16813-18-6]

Table 1. Experimental values with uncertainties. ρexp ± 2σ est

T K

293.15 273.15

Ref.

kg ⋅ m−3

837.0 ± 2.0 847.0 ± 2.0

19-wil/sch 19-wil/sch

8-Methyl-8-(2-methylpropyl)-6dodecanol

[500002-24-4]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

846.1 ± 2.0

Landolt-Börnstein New Series IV/8G

61-des/del

262

2.1.8 Alkanols, C13 - C22

3-Ethyl-3-hexadecanol

[900002-70-2]

C18H38O

MW = 270.5

494

C18H38O

MW = 270.5

495

C18H38O

MW = 270.5

496

Table 1. Experimental value with uncertainty. T K 295.95

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

840.5 ± 2.0

19-eyk

2-Heptyl-1-undecanol

[5333-44-8]

Table 1. Experimental value with uncertainty. T K 288.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

844.6 ± 2.0

38-mas

1-Octadecanol

[112-92-5]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 7.8077 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.5346 · 10−1 (combined temperature ranges, unweighted). T = 332.15 to 573.15 K ρ = A + BT + CT 2 + DT 3 + … 1.10078 · 103 −1.09517 9.79822 · 10−4 −8.62705 · 10−7

Coefficient A B C D

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 332.15 332.15 343.15 343.15 372.25 372.25 332.15 332.25 333.15 342.15 363.15 353.15 373.15 393.15

ρexp ± 2σ est −3

kg ⋅ m

812.40 ± 1.00 812.40 ± 2.00 804.80 ± 2.00 804.80 ± 1.00 784.90 ± 2.00 784.90 ± 1.00 813.30 ± 2.00 812.00 ± 3.00 813.00 ± 2.00 806.00 ± 2.00 792.00 ± 2.00 797.30 ± 1.00 783.90 ± 1.00 769.40 ± 1.00

ρexp − ρcalc kg ⋅ m−3

−1.10 −1.10 −0.69 −0.69 0.52 0.52 −0.20 −1.43 0.23 −0.22 1.03 −0.92 0.17 0.16

T K 1883-kra( ) 413.15 1883-kra( ) 433.15 1883-kra( ) 453.15 1883-kra( ) 473.15 1883-kra( ) 493.15 1883-kra( ) 513.15 533.15 1884-kra(∇) 49-tsv/mar(◆) 553.15 573.15 56-rat/cur(∆) 338.15 56-rat/cur(∆) 343.15 56-rat/cur(∆) 58-cos/bow( ) 348.15 58-cos/bow( ) 353.15 58-cos/bow( )

Ref. (Symbol in Fig. 1)

ρexp ± 2σ est −3

kg ⋅ m

754.50 ± 1.00 739.80 ± 1.00 725.10 ± 1.00 710.30 ± 1.00 695.60 ± 1.00 680.80 ± 1.00 666.10 ± 1.00 649.80 ± 1.00 631.60 ± 1.00 809.70 ± 0.60 805.60 ± 0.60 802.60 ± 0.60 799.50 ± 0.60

ρexp − ρcalc kg ⋅ m−3

−0.22 −0.33 −0.33 −0.27 0.08 0.57 1.44 1.02 −0.93 0.57 0.11 0.75 1.28

Ref. (Symbol in Fig. 1)

58-cos/bow( ) 58-cos/bow( ) 58-cos/bow( ) 58-cos/bow( ) 58-cos/bow( ) 58-cos/bow( ) 58-cos/bow( ) 58-cos/bow( ) 58-cos/bow( ) 92-lie/sen-1(✕ ) 92-lie/sen-1(✕ ) 92-lie/sen-1(✕ ) 92-lie/sen-1(✕ ) cont. Landolt-Börnstein New Series IV/8G

263

ρ

ρ

2.1.8 Alkanols, C13 - C22

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

330.00 340.00 350.00 360.00 370.00 380.00 390.00 400.00 410.00

Landolt-Börnstein New Series IV/8G

ρ ± σ fit kg ⋅ m−3 815.07 ± 1.73 807.78 ± 1.57 800.51 ± 1.45 793.25 ± 1.35 786.01 ± 1.27 778.76 ± 1.20 771.52 ± 1.14 764.27 ± 1.08 757.01 ± 1.03

T K

420.00 430.00 440.00 450.00 460.00 470.00 480.00 490.00 500.00

ρ ± σ fit kg ⋅ m−3 749.73 ± 0.98 742.44 ± 0.94 735.11 ± 0.92 727.75 ± 0.90 720.36 ± 0.91 712.92 ± 0.92 705.44 ± 0.94 697.91 ± 0.97 690.31 ± 1.01

T K

510.00 520.00 530.00 540.00 550.00 560.00 570.00 580.00

ρ ± σ fit kg ⋅ m−3 682.66 ± 1.06 674.93 ± 1.11 667.14 ± 1.16 659.26 ± 1.24 651.30 ± 1.34 643.25 ± 1.47 635.11 ± 1.65 626.87 ± 1.88

264

2.1.8 Alkanols, C13 - C22

3-Octadecanol

[26762-44-7]

C18H38O

MW = 270.5

497

C19H40O

MW = 284.53

498

C19H40O

MW = 284.53

499

C19H40O

MW = 284.53

500

C19H40O

MW = 284.53

501

C19H40O

MW = 284.53

502

Table 1. Experimental value with uncertainty. T K 353.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

785.8 ± 2.0

13-pic/ken

2,2-Dimethyl-3-(1,1-dimethylethyl)3-tridecanol

[500045-09-0]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

869.8 ± 1.5

60-pet/sok

7-Hexyl-7-tridecanol

[5340-59-0]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

840.8 ± 2.0

61-mes/erz

4-Methyl-4-octadecanol

[54892-13-6]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

839.4 ± 1.0

48-sor/sor

5-Methyl-5-octadecanol

[500020-99-5]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

837.4 ± 0.6

48-sor/sor

6-Methyl-6-octadecanol

[500021-00-1]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

838.5 ± 1.0

48-sor/sor

Landolt-Börnstein New Series IV/8G

2.1.8 Alkanols, C13 - C22 9-Methyl-9-octadecanol

[500021-01-2]

265

C19H40O

MW = 284.53

503

C20H42O

MW = 298.55

504

C20H42O

MW = 298.55

505

C20H42O

MW = 298.55

506

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

835.5 ± 1.0

48-sor/sor

1-Eicosanol

[629-96-9]

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 0.189. Coefficient ρ = A + BT 1056.70 A B −0.720 Table 2. Experimental values with uncertainties and deviation from calculated values. T K 348.15 358.15 368.15

ρexp ± 2σ est −3

kg ⋅ m

805.9 ± 0.50 798.7 ± 0.50 791.9 ± 0.50

ρexp − ρcalc

Ref.

kg ⋅ m−3

−0.13 −0.13 0.27

69-pat/kat 69-pat/kat 69-pat/kat

Table 3. Recommended values. ρexp ± 2σ est

T K 340.00 350.00 360.00 370.00

kg ⋅ m−3

811.9 ± 1.0 804.7 ± 0.6 797.5 ± 0.5 790.3 ± 0.8

3-Ethyl-3-octadecanol

[35185-53-6]

Table 1. Experimental value with uncertainty. T K 353.25

ρexp ± 2σ est

Ref.

kg ⋅ m−3

778.8 ± 3.0

19-eyk

2-Methyl-2-nonadecanol

[76695-48-2]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

352.95

Ref.

kg ⋅ m−3

771.7 ± 3.0

Landolt-Börnstein New Series IV/8G

19-eyk

266

2.1.8 Alkanols, C13 - C22

2-Octyl-1-dodecanol

[5333-42-6]

C20H42O

MW = 298.55

507

C20H42O

MW = 298.55

508

C22H46O

MW = 326.61

509

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 292.15 38-mas 846.3 ± 2.0 2,6,11,15-Tetramethyl-8-hexadecanol

[500002-33-5]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 292.15 23-von/kai 892.0 ± 2.0 1-Docosanol

[661-19-8]

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 0.094. Coefficient ρ = A + BT 1074.44 A B −0.770 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc ρexp ± 2σ est T Ref. −3 kg ⋅ m−3 K kg ⋅ m 348.15 69-pat/kat 806.3 ± 0.5 −0.07 358.15 69-pat/kat 798.6 ± 0.5 −0.07 368.15 0.13 69-pat/kat 791.1 ± 0.5 Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 340.00 812.6 ± 1.0 350.00 804.9 ± 0.6 3-Ethyl-3-eicosanol

ρexp ± 2σ est

T K

kg ⋅ m−3

797.2 ± 0.5 789.5 ± 0.7

360.00 370.00

[95287-47-1]

C22H46O

MW = 326.61

510

C22H46O

MW = 326.61

511

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 353.20 19-eyk 780.0 ± 3.0 2-Nonyl-1-tridecanol

[54439-52-0]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 290.65 847.6 ± 2.0 38-mas

Landolt-Börnstein New Series IV/8G

2.2.1 Alcohols of General Formula CnH2nO

267

2.2 Unsaturated Monoalcohols 2.2.1 Alcohols of General Formula CnH2nO 2-Propenol

[107-18-6]

C3H6O

MW = 58.08

512

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 8.0998 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.6309 · 10−1 (combined temperature ranges, unweighted). Coefficient A B C D

T = 273.15 to 440.00 K ρ = A + BT + CT 2 + DT 3 + … 1.05862 · 103 −1.61233 4.16485 · 10−3 −6.30190 · 10−6

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 273.15 799.50 ± 0.60 −1.02 1882-zan(✕ ) 293.15 786.00 ± 0.40 0.88 290.15 785.10 ± 0.60 −2.39 1882-zan1) 298.15 781.50 ± 0.40 0.39 283.15 794.00 ± 1.00 1.06 1890-gar1) 298.15 780.89 ± 0.20 −0.22 293.15 785.40 ± 1.00 0.28 1890-gar1) 298.15 780.80 ± 0.30 −0.31 303.15 776.50 ± 1.00 −0.52 1890-gar1) 298.15 780.81 ± 0.20 −0.30 313.15 767.50 ± 1.00 −1.12 1890-gar1) 298.15 780.86 ± 0.20 −0.25 323.15 758.20 ± 1.00 −1.65 1890-gar(✕ ) 293.15 785.50 ± 0.50 0.38 286.15 790.90 ± 0.60 0.28 19-eyk(✕ ) 313.15 768.40 ± 0.50 −0.22 273.15 799.90 ± 0.60 −0.62 25-pal/con(✕ ) 333.15 749.70 ± 0.50 −1.01 355.35 728.30 ± 0.70 −0.51 27-arb-2(✕ ) 298.15 780.90 ± 0.30 −0.21 355.35 728.40 ± 0.70 -0.41 27-arb-2(✕ ) 293.15 785.40 ± 0.30 0.28 356.45 727.70 ± 0.70 0.03 27-arb-2(✕ ) 300.00 779.00 ± 1.00 −0.61 356.45 727.70 ± 0.70 0.03 27-arb-2(✕ ) 320.00 763.00 ± 1.00 0.35 273.15 801.34 ± 0.60 0.82 34-tim/del(✕ ) 340.00 745.00 ± 1.00 0.81 288.15 789.14 ± 0.60 0.08 34-tim/del1) 360.00 724.00 ± 1.00 0.08 303.15 776.88 ± 0.60 −0.14 34-tim/del1) 380.00 702.00 ± 1.00 0.46 308.15 772.21 ± 0.60 −0.65 43-lan/key(✕ ) 400.00 676.00 ± 1.50 −0.74 293.15 786.40 ± 0.60 1.28 48-vog-21) 420.00 648.00 ± 1.50 −1.23 314.35 769.70 ± 0.60 2.12 48-vog-2(✕ ) 440.00 619.00 ± 1.50 0.31 332.35 753.20 ± 0.60 1.75 48-vog-2(✕ ) 460.00 585.00 ± 1.50 0.17 296.15 783.84 ± 0.30 1.12 51-dim/lan(✕ ) 480.00 541.00 ± 2.00 −6.34 288.15 790.00 ± 0.40 0.94 52-cap/mug(✕ ) 500.00 470.00 ± 2.00 −35.93 1)

Ref. (Symbol in Fig. 1) 52-cap/mug1) 52-cap/mug1) 52-wil/sim( ) 54-bre(◆) 54-kre/wie(∆) 54-pur/bow( ) 56-tor-11) 56-tor-1(✕ ) 56-tor-1(✕ ) 58-arn/was(✕ ) 63-amb/tow(∇) 64-dan/bah1) 64-dan/bah(✕ ) 64-dan/bah(✕ ) 64-dan/bah(✕ ) 64-dan/bah(✕ ) 64-dan/bah(✕ ) 64-dan/bah(✕ ) 64-dan/bah(✕ ) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1)

Not included in Fig. 1.

cont.

Landolt-Börnstein New Series IV/8G

268

2.2.1 Alcohols of General Formula CnH2nO

2-Propenol (cont.)

ρ

ρ

Further references: [1872-lin/von, 1880-bru-1, 1880-bru-3, 1880-tho, 1881-pri/han, 1882-sch-1, 1883-sch-3, 1884-gla, 1884-per, 1884-sch-6, 1897-tho, 02-you/for, 08-dor/dvo, 13-atk/wal, 14-vav, 21-leb, 23-clo/joh, 25-nor/ash, 25-par/kel, 25-par/kel-1, 25-rak, 27-par/cha, 28-par/bar, 28-par/nel, 29-ber, 29-ber/reu, 29-swa, 31-ton/ueh, 33-tre/wat, 35-hen, 35-mah-1, 35-ols/was, 37-zep, 38-dol/gre, 40-mil/bli, 40-was/beg, 40-was/gra, 42-sch/hun, 42-was/bro, 43-bru/bog, 43-dur/roe, 48-wei, 49-hat, 50-jac, 50-par/gol, 50-pic/zie, 52-coo, 53-ani, 53-ani-1, 57-rom-1, 58-hil/hay, 61-ogi/cor, 62-bro/smi, 63-lab].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15 298.15 300.00 310.00

ρ ± σ fit kg ⋅ m−3 802.87 ± 0.67 795.35 ± 0.56 787.61 ± 0.50 785.12 ± 0.50 781.11 ± 0.49 779.61 ± 0.49 771.30 ± 0.50

T K

320.00 330.00 340.00 350.00 360.00 370.00 380.00

ρ ± σ fit kg ⋅ m−3 762.65 ± 0.53 753.63 ± 0.58 744.19 ± 0.65 734.30 ± 0.73 723.92 ± 0.83 713.02 ± 0.95 701.54 ± 1.08

T K

390.00 400.00 410.00 420.00 430.00 440.00 450.00

ρ ± σ fit kg ⋅ m−3 689.46 ± 1.24 676.74 ± 1.41 663.34 ± 1.62 649.23 ± 1.86 634.35 ± 2.16 618.69 ± 2.52 602.19 ± 2.96

Landolt-Börnstein New Series IV/8G

2.2.1 Alcohols of General Formula CnH2nO 1-Buten-3-ol

[598-32-3]

269

C4H8O

MW = 72.11

513

C4H8O

MW = 72.11

514

C5H10O

MW = 86.13

515

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 52-wib 830.0 ± 2.0

(Z)-2-Buten-1-ol

[4088-60-2]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 58-hil/hay 895.0 ± 3.0

2-Methyl-3-buten-2-ol

[115-18-4]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 3.3193 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.9173 · 10−1 (combined temperature ranges, unweighted). T = 293.15 to 343.15 K ρ = A + BT + CT 2 + DT 3 + … 8.68886 · 102 5.71276 · 10−1 −2.47190 · 10−3

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc Ref. (Symbol ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) in Fig. 1) ⋅ kg m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 293.15 824.80 ± 1.00 0.87 41-cam/eby-1( ) 323.15 795.00 ± 0.50 −0.36 88-bag/gur(✕ ) 293.15 823.40 ± 0.50 −0.53 88-bag/gur(✕ ) 333.15 784.60 ± 0.50 −0.25 88-bag/gur(✕ ) 303.15 814.90 ± 0.50 −0.00 88-bag/gur(✕ ) 343.15 773.90 ± 0.50 0.05 88-bag/gur(✕ ) 313.15 805.60 ± 0.50 0.22 88-bag/gur(✕ )

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

290.00 293.15 298.15

ρ ± σ fit kg ⋅ m−3 826.67 ± 0.97 823.93 ± 0.84 819.48 ± 0.67

T K

300.00 310.00 320.00

ρ ± σ fit kg ⋅ m−3 817.80 ± 0.63 808.43 ± 0.51 798.57 ± 0.48

T K

330.00 340.00 350.00

ρ ± σ fit kg ⋅ m−3 788.22 ± 0.51 777.37 ± 0.70 766.02 ± 1.13 cont.

Landolt-Börnstein New Series IV/8G

270

2.2.1 Alcohols of General Formula CnH2nO

ρ

ρ

2-Methyl-3-buten-2-ol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

1-Penten-3-ol

[616-25-1]

C5H10O

MW = 86.13

516

C5H10O

MW = 86.13

517

C5H10O

MW = 86.13

518

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 63-lab 833.0 ± 0.6 3-Penten-1-ol

[39161-19-8]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 48-goe/cri 849.2 ± 1.0 4-Penten-1-ol

[821-09-0]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 298.15 45-sch/gel 839.5 ± 1.0 Landolt-Börnstein New Series IV/8G

2.2.1 Alcohols of General Formula CnH2nO (E)-3,3-Dimethyl-2-buten-1-ol

[500029-65-2]

271

C6H12O

MW = 100.16

519

C6H12O

MW = 100.16

520

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 0.047. Coefficient ρ = A + BT A 1037.77 B −0.700 Table 2. Experimental values with uncertainties and deviation from calculated values. T K

293.15 298.15 303.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m

kg ⋅ m−3

−3

832.5 ± 0.7 829.1 ± 0.7 825.6 ± 0.7

Ref.

−0.07 0.03 0.03

61-hat/wei 61-hat/wei 61-hat/wei

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 290.00 834.8 ± 0.7 293.15 832.6 ± 0.7 298.15 829.1 ± 0.6 310.00 820.8 ± 0.9 (Z)-3,3-Dimethyl-2-buten-1-ol

[500029-64-1]

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 0.094. Coefficient ρ = A + BT A 1041.21 B −0.680 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

293.15 298.15 303.15

−3

kg ⋅ m

841.8 ± 0.7 838.4 ± 0.7 835.2 ± 0.7

ρexp − ρcalc kg ⋅ m

−0.07 −0.07 0.13

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 290.00 844.0 ± 0.8 293.15 841.9 ± 0.7 298.15 838.5 ± 0.6 310.00 830.4 ± 0.9

Landolt-Börnstein New Series IV/8G

Ref.

−3

61-hat/wei 61-hat/wei 61-hat/wei

272

2.2.1 Alcohols of General Formula CnH2nO

1-Hexen-3-ol

[4798-44-1]

C6H12O

MW = 100.16

521

C6H12O

MW = 100.16

522

C6H12O

MW = 100.16

523

C6H12O

MW = 100.16

524

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 63-lab 835.7 ± 0.6 2-Hexen-1-ol

[500026-97-1]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 288.15 30-wal/ros 850.8 ± 1.0 (E)-2-Hexen-1-ol

[928-95-0]

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 0.094. Coefficient ρ = A + BT A 1039.35 B −0.640 Table 2. Experimental values with uncertainties and deviation from calculated values. T K 293.15 298.15 303.15

ρexp ± 2σ est kg ⋅ m

−3

851.6 ± 0.7 848.6 ± 0.7 845.4 ± 0.7

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−0.13 0.07 0.07

61-hat/wei 61-hat/wei 61-hat/wei

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 290.00 853.7 ± 0.8 293.15 851.7 ± 0.7 298.15 848.5 ± 0.6 310.00 840.9 ± 0.9 2-Hexen-4-ol

[4798-58-7]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 54-gay/cro1) 836.7 ± 1.0 293.15 63-lab 841.6 ± 0.6 293.15 Recommended 841.6 ± 0.6 1)

Not included in calculation of recommended value.

Landolt-Börnstein New Series IV/8G

2.2.1 Alcohols of General Formula CnH2nO 5-Hexen-2-ol

[626-94-8]

273

C6H12O

MW = 100.16

525

C6H12O

MW = 100.16

526

C6H12O

MW = 100.16

527

C6H12O

MW = 100.16

528

C6H12O

MW = 100.16

529

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 297.15 49-col/lag 838.0 ± 2.0 2-Methyl-1-penten-3-ol

[2088-07-5]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 65-col/des 840.0 ± 2.0 2-Methyl-2-penten-1-ol

[1610-29-3]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 298.15 65-col/des 851.0 ± 2.0 3-Methyl-1-penten-3-ol

[918-85-4]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 298.15 52-mye/col 833.4 ± 0.5 3-Methyl-2-penten-1-ol

[500060-37-7]

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.380. Coefficient ρ = A + BT A 1078.78 B −0.780 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc ρexp ± 2σ est T Ref. −3 −3 kg ⋅ m K kg ⋅ m 273.15 0.38 50-fav/fri 866.1 ± 1.5 291.15 50-fav/fri 851.3 ± 1.5 −0.38 Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 270.00 868.2 ± 1.5 280.00 860.4 ± 1.4 290.00 852.6 ± 1.4

Landolt-Börnstein New Series IV/8G

T K 293.15 298.15

ρexp ± 2σ est kg ⋅ m−3

850.1 ± 1.5 846.2 ± 1.6

274

2.2.1 Alcohols of General Formula CnH2nO

3-Methyl-4-penten-3-ol

[500060-36-6]

C6H12O

MW = 100.16

530

C7H14O

MW = 114.19

531

C7H14O

MW = 114.19

532

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 2.090. Coefficient ρ = A + BT A 1096.92 B −0.860 Table 2. Experimental values with uncertainties and deviation from calculated values. T K

273.15 295.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m

kg ⋅ m−3

−3

864.1 ± 1.5 841.0 ± 1.5

Ref.

2.09 −2.09

50-fav/fri 50-fav/fri

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 270.00 864.7 ± 2.9 280.00 856.1 ± 2.5 290.00 847.5 ± 2.6 293.15 844.8 ± 2.6 298.15 840.5 ± 2.9

2-Hepten-4-ol

[4798-59-8]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 63-lab 844.5 ± 0.6

(Z)-3-Hepten-1-ol

[1708-81-2]

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 0.249. Coefficient ρ = A + BT A 1064.56 B −0.740 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc ρexp ± 2σ est T Ref. −3 kg ⋅ m−3 K kg ⋅ m 293.15 0.27 61-hat/wei 847.9 ± 0.7 298.15 61-hat/wei 843.6 ± 0.7 −0.33 303.15 0.07 61-hat/wei 840.3 ± 0.7 cont.

Landolt-Börnstein New Series IV/8G

2.2.1 Alcohols of General Formula CnH2nO

275

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 290.00 850.0 ± 0.8 293.15 847.6 ± 0.7 298.15 843.9 ± 0.7 310.00 835.2 ± 0.9 4-Hepten-1-ol

[20851-55-2]

C7H14O

MW = 114.19

533

C7H14O

MW = 114.19

534

C7H14O

MW = 114.19

535

C7H14O

MW = 114.19

536

C7H14O

MW = 114.19

537

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 64-ber/vav 844.3 ± 2.0 5-Hepten-1-ol

[89794-36-5]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 291.15 56-gla/gau 846.1 ± 1.0 2-Methyl-1-hexen-3-ol

[500029-09-4]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 65-col/des 842.0 ± 2.0 2-Methyl-2-hexen-1-ol

[500029-07-2]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 65-col/des 846.0 ± 2.0 3-Methyl-1-hexen-3-ol

[55145-28-3]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 290.15 46-shi 836.7 ± 1.0

Landolt-Börnstein New Series IV/8G

276

2.2.1 Alcohols of General Formula CnH2nO

4-Methyl-1-hexen-4-ol

[500005-96-9]

C7H14O

MW = 114.19

538

C7H14O

MW = 114.19

539

C7H14O

MW = 114.19

540

C8H16O

MW = 128.21

541

C8H16O

MW = 128.21

542

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 63-lab 827.0 ± 0.6 4-Methyl-4-hexen-3-ol

[101084-24-6]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 298.15 50-pau/tch 856.0 ± 2.0 5-Methyl-2-hexen-4-ol

[500025-43-4]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 63-lab 842.0 ± 0.6 1,1-Dimethyl-5-hexen-1-ol

[77437-98-0]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 55-che/che 842.3 ± 1.0 3,5-Dimethyl-4-hexen-3-ol

[1569-43-3]

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.298. Coefficient ρ = A + BT A 1098.38 B −0.820 Table 2. Experimental values with uncertainties and deviation from calculated values. T K 273.15 290.35

ρexp ± 2σ est −3

kg ⋅ m

874.7 ± 2.0 860.0 ± 2.0

ρexp − ρcalc

Ref.

kg ⋅ m−3

0.30 −0.30

34-jac-6 34-jac-6

cont.

Landolt-Börnstein New Series IV/8G

2.2.1 Alcohols of General Formula CnH2nO

277

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 270.00 877.0 ± 1.9 280.00 868.8 ± 1.8 290.00 860.6 ± 1.9 293.15 858.0 ± 1.9 298.15 853.9 ± 2.0 3-Ethyl-5-hexen-2-ol

[60091-37-4]

C8H16O

MW = 128.21

543

C8H16O

MW = 128.21

544

C8H16O

MW = 128.21

545

C8H16O

MW = 128.21

546

C9H18O

MW = 142.24

547

Table 1. Experimental values with uncertainties. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 289.45 47-col/lag 854.0 ± 2.0 289.15 49-col/lag 854.0 ± 2.0 6-Methyl-3-hepten-2-ol

[51500-48-2]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 62-mir/fed 830.1 ± 2.0 6-Methyl-5-hepten-2-ol

[1569-60-4]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 62-mir/fed 858.8 ± 2.0 2-Octen-4-ol

[4798-61-2]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 63-lab 847.5 ± 0.6 2,2-Dimethyl-6-hepten-3-ol

[54525-85-8]

Table 1. Experimental values with uncertainties. ρexp ± 2σ est T Ref. K kg ⋅ m−3 294.15 47-col/lag 843.0 ± 2.0 297.15 49-col/lag 843.0 ± 2.0

Landolt-Börnstein New Series IV/8G

278

2.2.1 Alcohols of General Formula CnH2nO

2,4-Dimethyl-2-hepten-4-ol

[59673-20-0]

C9H18O

MW = 142.24

548

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.176. Coefficient ρ = A + BT A 1076.98 B −0.780 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc ρexp ± 2σ est T Ref. −3 −3 ⋅ kg m K kg ⋅ m 273.15 0.18 34-jac-6 864.1 ± 2.0 289.75 34-jac-6 850.8 ± 2.0 −0.18 Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 270.00 866.4 ± 1.9 280.00 858.6 ± 1.8 290.00 850.8 ± 1.8 (E)-2-Methyl-3-octen-2-ol

[18521-06-7]

C9H18O

MW = 142.24

549

C9H18O

MW = 142.24

550

C9H18O

MW = 142.24

551

C9H18O

MW = 142.24

552

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 41-cam/eby-1 830.1 ± 0.5 (Z)-2-Methyl-3-octen-2-ol

[18521-07-8]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 41-cam/eby-1 837.8 ± 0.5 4-Methyl-3-octen-5-ol

[500025-37-6]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 12-bje 846.8 ± 0.8 4-Methyl-4-octen-1-ol

[500000-06-6]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 50-pau/tch 852.0 ± 2.0 Landolt-Börnstein New Series IV/8G

2.2.1 Alcohols of General Formula CnH2nO 2,4-Dimethyl-2-octen-4-ol

[76008-28-1]

C10H20O

279 MW = 156.27

553

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.120. Coefficient ρ = A + BT A 1078.70 B −0.800 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc ρexp ± 2σ est T Ref. −3 −3 ⋅ kg m K kg ⋅ m 273.15 0.12 34-jac-6 860.3 ± 2.0 292.35 34-jac-6 844.7 ± 2.0 −0.12 Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 270.00 862.7 ± 1.9 280.00 854.7 ± 1.8 290.00 846.7 ± 1.8 293.15 844.2 ± 1.9 298.15 840.2 ± 2.0 3,5-Dimethyl-6-octen-2-ol

[57785-04-3]

C10H20O

MW = 156.27

554

C10H20O

MW = 156.27

555

C10H20O

MW = 156.27

556

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 864.00 ± 1.00 75-lee/che 3,7-Dimethyl-6-octen-1-ol

[106-22-9]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est

T K

293.15 293.15 293.15 1)

Ref.

kg ⋅ m−3

890.0 ± 6.0 865.3 ± 1.0 865.3 ± 1.0

1884-gla1) 54-ser/voi-1 Recommended

Not included in calculation of recommended value.

2,2,3-Trimethyl-6-hepten-3-ol

[85924-69-2]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 294.15 862.0 ± 2.0 49-col/lag

Landolt-Börnstein New Series IV/8G

280

2.2.1 Alcohols of General Formula CnH2nO

2,3,4-Trimethyl-5-hepten-2-ol

[57785-05-4]

C10H20O

MW = 156.27

557

C11H22O

MW = 170.30

558

C12H24O

MW = 184.32

559

C18H36O

MW = 268.48

560

C18H36O

MW = 268.48

561

C19H38O

MW = 282.51

562

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 75-lee/che 875.0 ± 1.0

3-Ethyl-1-nonen-4-ol

[10544-97-5]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 65-mig/mig 843.0 ± 2.0

3,4,8-Trimethyl-1-nonen-3-ol

[18352-66-4]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 67-min/che 852.1 ± 1.0

(E)-9-Octadecen-1-ol

[506-42-3]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 313.15 26-boe/bel 833.8 ± 1.0

(Z)-9-Octadecen-1-ol

[143-28-2]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 313.15 26-boe/bel 836.7 ± 1.0

3,7,11-Trimethyl-2-hexadecen-1-ol

[102013-46-7]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 60-naz/mak 856.1 ± 2.0

Landolt-Börnstein New Series IV/8G

2.2.1 Alcohols of General Formula CnH2nO 3,7,11,15-Tetramethyl-1-hexadecen-3-ol

[60046-87-9]

C20H40O

281 MW = 296.54

563

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 2.9464 · 10−1 (combined temperature ranges, weighted), σc,uw = 8.4869 · 10−2 (combined temperature ranges, unweighted). Coefficient A B

T = 293.15 to 343.15 K ρ = A + BT + CT 2 + DT 3 + … 1.06651 · 103 −7.53664 · 10−1

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc Ref. (Symbol ρexp ± 2σ est ρexp ± 2σ est T T in Fig. 1) in Fig. 1) kg ⋅ m−3 kg ⋅ m−3 K K kg ⋅ m−3 kg ⋅ m−3 293.15 845.40 ± 0.60 −0.18 62-mau/smi( ) 293.15 845.80 ± 0.50 0.22 88-bag/gur( ) 293.15 845.80 ± 0.50 0.22 303.15 837.80 ± 0.50 −0.24 88-bag/gur( ) 85-bel/ber(∆) 303.15 837.80 ± 0.50 −0.24 313.15 830.50 ± 0.50 −0.00 88-bag/gur( ) 85-bel/ber(∆) 313.15 830.50 ± 0.50 −0.00 323.15 822.80 ± 0.50 −0.17 88-bag/gur( ) 85-bel/ber(∆) 323.15 822.80 ± 0.50 −0.17 333.15 816.00 ± 0.50 0.57 88-bag/gur( ) 85-bel/ber(∆) 333.15 816.00 ± 0.50 0.57 343.15 807.60 ± 0.50 −0.29 88-bag/gur( ) 85-bel/ber(∆) 343.15 807.60 ± 0.50 −0.29 85-bel/ber(∆)

ρ

ρ

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont. Landolt-Börnstein New Series IV/8G

282

2.2.1 Alcohols of General Formula CnH2nO

3,7,11,15-Tetramethyl-1-hexadecen-3-ol (cont.) Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

290.00 293.15 298.15

ρ ± σ fit kg ⋅ m−3 847.95 ± 0.65 845.58 ± 0.62 841.81 ± 0.58

3,7,11,15-Tetramethyl2-heptadecen-1-ol,

ρ ± σ fit kg ⋅ m−3

T K

840.41 ± 0.56 832.88 ± 0.47 825.34 ± 0.43

300.00 310.00 320.00

[114161-31-8]

T K

330.00 340.00 350.00

ρ ± σ fit kg ⋅ m−3 817.80 ± 0.47 810.27 ± 0.61 802.73 ± 0.89

C21H42O

MW = 310.56

564

C23H46O

MW = 338.62

565

C23H46O

MW = 338.62

566

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 60-naz/mak 858.6 ± 2.0

3,7,11,15,16,16-Hexamethyl1-heptadecen-3-ol

[113058-51-8]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 60-naz/mak 851.9 ± 2.0

3,7,11,15,16,16-Hexamethyl2-heptadecen-1-ol

[113057-97-9]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 60-naz/mak 862.8 ± 2.0

Landolt-Börnstein New Series IV/8G

2.2.2 Alcohols of General Formula CnH2n-2O

283

2.2.2 Alcohols of General Formula CnH2n-2O 2-Propyn-1-ol

[107-19-7]

C3H4O

MW = 56.06

567

Table 1. Experimental and recommended values with uncertainties. T K 293.15 291.95 294.15 293.15 1)

ρexp ± 2σ est

T K 293.15 293.15 298.15 298.15

Ref.

kg ⋅ m−3

971.5 ± 5.00 971.0 ± 5.00 972.8 ± 5.00 983.5 ± 5.00

1880-bru-31) 1880-bru-31) 1880-bru-31) 1880-bru-31)

ρexp ± 2σ est

Ref.

kg ⋅ m−3

983.5 ± 5.00 947.6 ± 1.00 945.2 ± 0.60 945.2 ± 0.60

1880-bru-31) 45-hen/gre1) 95-kum/rao-1 Recommended

Not included in calculation of recommended value.

3-Butyn-1-ol

[927-74-2]

C4H6O

MW = 70.09

568

C5H8O

MW = 84.12

569

C5H8O

MW = 84.12

570

C5H8O

MW = 84.12

571

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

925.5 ± 0.5

45-hen/gre

2-Methyl-3-butyn-2-ol

[115-19-5]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est

T K

293.15 293.15 293.15 293.15 1)

Ref.

−3

kg ⋅ m

861.3 ± 0.6 861.2 ± 0.6 865.8 ± 2.0 861.3 ± 0.6

41-cam/eby-1 45-hen/gre 62-mau/smi1) Recommended

Not included in calculation of recommended value.

3,4-Pentadien-2-ol

[17615-19-9]

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

901.4 ± 2.0

62-ber/leg-1

2-Pentyn-1-ol

[6261-22-9]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

−3

kg ⋅ m

907.7 ± 1.0

Landolt-Börnstein New Series IV/8G

64-zak/sta

284

2.2.2 Alcohols of General Formula CnH2n-2O

4-Pentyn-1-ol

[5390-04-5]

C5H8O

MW = 84.12

572

C5H8O

MW = 84.12

573

C6H10O

MW = 98.14

574

C6H10O

MW = 98.14

575

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

913.2 ± 2.0

55-mos

(RS)-4-Pentyn-2-ol

[2117-11-5]

Table 1. Experimental and recommended values with uncertainties. T K 293.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

895.7 ± 0.6 905.0 ± 2.0 895.7 ± 0.6

54-pom/foo 62-ber/leg-11) Recommended

Not included in calculation of recommended value.

3,3-Dimethyl-2-butyn-1-ol

[500029-63-0]

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 0.047. Coefficient ρ = A + BT 1074.80 A B −0.740 Table 2. Experimental values with uncertainties and deviation from calculated values. T K 293.15 298.15 303.15

ρexp ± 2σ est

ρexp − ρcalc

Ref.

kg ⋅ m−3

−3

kg ⋅ m

857.8 ± 0.7 854.2 ± 0.7 850.5 ± 0.7

−0.07 0.03 0.03

61-hat/wei 61-hat/wei 61-hat/wei

Table 3. Recommended values. T K 290.00 293.15

ρexp ± 2σ est

ρexp ± 2σ est

T K 298.15 310.00

−3

kg ⋅ m

860.2 ± 0.7 857.9 ± 0.7

4,5-Hexadien-3-ol

kg ⋅ m−3

854.2 ± 0.6 845.4 ± 0.9 [4376-43-6]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

880.7 ± 2.0

62-ber/leg-1

Landolt-Börnstein New Series IV/8G

2.2.2 Alcohols of General Formula CnH2n-2O 5-Hexyn-1-ol

[928-90-5]

285

C6H10O

MW = 98.14

576

C6H10O

MW = 98.14

577

C7H12O

MW = 112.17

578

C7H12O

MW = 112.17

579

C7H12O

MW = 112.17

580

C7H12O

MW = 112.17

581

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

902.0 ± 1.0

64-zak/sta

5-Hexyn-3-ol

[19780-84-8]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

893.1 ± 2.0

62-ber/leg-1

3-Ethyl-1-pentyn-3-ol

[6285-06-9]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

kg ⋅ m−3

871.7 ± 0.6

45-hen/gre

1,2-Heptadien-4-ol

[4376-46-9]

Table 1. Experimental value with uncertainty. T K 294.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

868.8 ± 2.0

62-ber/leg-1

1-Heptyn-4-ol

[22127-83-9]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

291.15

Ref.

kg ⋅ m−3

886.7 ± 2.0

2-Heptyn-1-ol

62-ber/leg-1

[1002-36-4]

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 0.062. Coefficient ρ = A + BT 1106.75 A B −0.750 cont. Landolt-Börnstein New Series IV/8G

286

2.2.2 Alcohols of General Formula CnH2n-2O

2-Heptyn-1-ol (cont.) Table 2. Experimental values with uncertainties and deviation from calculated values. T K

293.15 298.15 303.15 293.15 1)

ρexp ± 2σ est

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−3

kg ⋅ m

886.8 ± 0.7 883.2 ± 0.7 879.4 ± 0.7 885.8 ± 1.0

−0.08 0.07 0.02 −1.08

61-hat/wei 61-hat/wei 61-hat/wei 64-zak/sta1)

Not included in calculation of linear coefficients.

Table 3. Recommended values. T K

290.00 293.15 298.15 310.00

ρexp ± 2σ est kg ⋅ m−3

889.2 ± 0.6 886.9 ± 0.5 883.1 ± 0.5 874.2 ± 0.8

2-Methyl-3,5-hexadien-2-ol

[926-38-5]

C7H12O

MW = 112.17

582

C7H12O

MW = 112.17

583

C7H12O

MW = 112.17

584

C7H12O

MW = 112.17

585

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

864.9 ± 2.0

64-bog/kug

2-Methyl-4,5-hexadien-3-ol

[4376-49-2]

Table 1. Experimental value with uncertainty. T K 294.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

872.2 ± 2.0

62-ber/leg-1

5-Methyl-3,5-hexadien-1-ol

[19764-79-5]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

889.9 ± 1.0

67-min/che

2-Methyl-5-hexyn-3-ol

[54838-77-6]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

874.9 ± 2.0

62-ber/leg-1

Landolt-Börnstein New Series IV/8G

2.2.2 Alcohols of General Formula CnH2n-2O 3-Methyl-1-hexyn-3-ol

[4339-05-3]

287

C7H12O

MW = 112.17

586

C8H14O

MW = 126.2

587

C8H14O

MW = 126.20

588

C8H14O

MW = 126.20

589

C8H14O

MW = 126.20

590

C9H16O

MW = 140.23

591

C9H16O

MW = 140.23

592

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 290.15 46-shi 867.1 ± 1.0 3,5-Dimethyl-1-hexyn-3-ol

[107-54-0]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 57-hic/ken 858.2 ± 1.0 2-Methyl-2,3-heptadien-1-ol

[14270-80-5]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 66-per/bal 875.1 ± 1.0 3-Methyl-1,6-heptadien-4-ol

[1838-74-0]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 298.15 65-col/des 868.0 ± 1.0 5-Methyl-3,5-heptadien-1-ol

[19756-78-6]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 67-min/che 898.2 ± 1.0 2,6-Dimethyl-3-heptyn-5-ol

[5923-00-2]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 65-fav/nik 848.2 ± 2.0 3-Methyl-3,4-octadien-2-ol

[14270-81-6]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 66-per/bal 860.2 ± 1.0 Landolt-Börnstein New Series IV/8G

288

2.2.2 Alcohols of General Formula CnH2n-2O

5-Methyl-3,5-octadien-1-ol

[19756-79-7]

C9H16O

MW = 140.23

593

C9H16O

MW = 140.23

594

C9H16O

MW = 140.23

595

C9H16O

MW = 140.23

596

C9H16O

MW = 140.23

597

C9H16O

MW = 140.23

598

C 10H18O

MW = 154.25

599

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 67-min/che 890.2 ± 1.0 6-Methyl-2,6-octadien-8-ol

[900002-84-8]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 60-naz/mak 877.0 ± 2.0 2-Methyl-3-octyn-2-ol

[20599-16-0]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 41-cam/eby-1 850.6 ± 0.5 2-Methyl-3-octyn-5-ol

[5922-99-6]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 65-fav/nik 851.8 ± 2.0 5,8-Nonadien-2-ol

[13175-61-6]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 63-col/bue 1086.5 ± 2.0 4-Nonyn-3-ol

[999-70-2]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 63-lab 866.1 ± 0.7 2,3-Dimethyl-3,4-octadien-2-ol

[14129-51-2]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 66-per/bal 867.8 ± 1.0 Landolt-Börnstein New Series IV/8G

2.2.2 Alcohols of General Formula CnH2n-2O (E)-3,7-Dimethyl-2,6-octadien-1-ol

[106-24-1]

289

C10H18O

MW = 154.25

600

C10H18O

MW = 154.25

601

C10H18O

MW = 154.25

602

C10H18O

MW = 154.25

603

C10H18O

MW = 154.25

604

C11H20O

MW = 168.28

605

C11H20O

MW = 168.28

606

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 298.15 65-rum 879.2 ± 0.7 (Z)-3,7-Dimethyl-2,6-octadien-1-ol

[106-25-2]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 298.15 65-rum 873.3 ± 0.7 3,7-Dimethyl-1-octyn-3-ol

[1604-26-8]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 62-mau/smi 852.1 ± 2.0 8-Methyl-5,8-nonadien-2-ol

[13175-62-7]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 298.15 63-col/bue 882.0 ± 2.0 3-Propyl-1,2-heptadien-4-ol

[900002-85-9]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 297.15 62-ber/leg-1 863.2 ± 2.0 3,5-Diethyl-1,6-heptadine-4-ol

[10545-05-8]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 65-mig/mig 892.0 ± 2.0 3,7-Dimethyl-2,6-nonadien-1-ol

[41865-30-9]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 60-naz/mak 881.0 ± 2.0 Landolt-Börnstein New Series IV/8G

290

2.2.2 Alcohols of General Formula CnH2n-2O

3-Ethenyl-1-nonen-4-ol

[13014-73-8]

C11H20O

MW = 168.28

607

C11H20O

MW = 168.28

608

C12H22O

MW = 182.31

609

C12H22O

MW = 182.31

610

C13H24O

MW = 196.33

611

C13H24O

MW = 196.33

612

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 65-mig/mig 854.0 ± 2.0 10-Undecyn-1-ol

[2774-84-7]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 62-ber/mol 873.3 ± 1.0 3,4,8-Trimethyl-1-nonyn-3-ol

[18352-64-2]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 67-min/che 858.6 ± 1.0 3,7,8-Trimethyl-2,6-nonadien-1-ol

[105906-02-3]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 60-naz/mak 879.5 ± 2.0 2,8-Dimethyl-3-ethyl-3,4-nonadien-2-ol

[14270-84-9]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 66-per/bal 830.0 ± 1.0 3-(1,1-Dimethylethyl)-2-methyl3,4-octadien-2-ol

[14129-52-3]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 66-per/bal 833.9 ± 1.0

Landolt-Börnstein New Series IV/8G

2.2.2 Alcohols of General Formula CnH2n-2O 3-Ethyl-2,7,7-trimethyl-3,4-octadien-2-ol

291

[14270-83-8]

C13H24O

MW = 196.33

613

[1846-65-7]

C 13H24O

MW = 196.33

614

[92857-08-4]

C15H28O

MW = 224.39

615

[1604-35-9]

C 15H28O

MW = 224.39

616

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 849.3 ± 1.0 66-per/bal

5-Tridecyn-7-ol Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15

854.6 ± 0.6

63-lab

5-Pentadecyn-7-ol Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15

853.6 ± 0.7

63-lab

3,7,11-Trimethyl-1-dodecyn-3-ol

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 3.7211 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.5548 · 10−1 (combined temperature ranges, unweighted).

T = 293.00 to 343.15 K ρ = A + BT + CT 2 + DT 3 + … 1.07542 · 103 −7.63342 · 10−1

Coefficient A B

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T in Fig. 1) kg ⋅ m−3 kg ⋅ m−3 K K kg ⋅ m−3 kg ⋅ m−3 293.15 293.00 293.15 303.15

851.00 ± 1.00 851.90 ± 0.50 851.90 ± 0.50 844.10 ± 0.50

−0.65 0.14 0.25 0.09

62-mau/smi( ) 86-bae(✕ ) 88-bag/gur( ) 88-bag/gur( )

313.15 323.15 333.15 343.15

836.10 ± 0.50 828.80 ± 0.50 821.90 ± 0.50 813.10 ± 0.50

−0.28 0.05 0.79 −0.38

Ref. (Symbol in Fig. 1)

) ) ) )

88-bag/gur( 88-bag/gur( 88-bag/gur( 88-bag/gur(

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ).

T K 290.00 293.15 298.15

ρ ± σ fit kg ⋅ m−3 854.05 ± 0.73 851.65 ± 0.70 847.83 ± 0.64

T K 300.00 310.00 320.00

ρ ± σ fit kg ⋅ m−3 846.42 ± 0.62 838.79 ± 0.50 831.15 ± 0.43

T K 330.00 340.00 350.00

ρ ± σ fit kg ⋅ m−3 823.52 ± 0.47 815.89 ± 0.64 808.25 ± 0.97

cont.

Landolt-Börnstein New Series IV/8G

292

2.2.2 Alcohols of General Formula CnH2n-2O

ρ

ρ

3,7,11-Trimethyl-1-dodecyn-3-ol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

9,12-Octadecadien-1-ol

[1577-52-2]

C18H34O

MW = 266.47

617

C20H38O

MW = 294.52

618

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

861.2 ± 1.0

38-tur

3,7,11,15-Tetramethyl-1-hexadecyn-3-ol

[29171-23-1]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 4.5296 · 10−1 (combined temperature ranges, weighted), σc,uw = 2.9444 · 10−1 (combined temperature ranges, unweighted). Coefficient A B

T = 293.15 to 343.15 K ρ = A + BT + CT 2 + DT 3 + … 1.06610 · 103 −7.31308 · 10−1 cont.

Landolt-Börnstein New Series IV/8G

2.2.2 Alcohols of General Formula CnH2n-2O

293

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

kg ⋅ m

Ref. (Symbol in Fig. 1)

853.30 ± 2.00 851.70 ± 0.50 843.90 ± 0.50 836.80 ± 0.50

1.59 −0.01 −0.50 −0.29

62-mau/smi( 88-bag/gur( 88-bag/gur( 88-bag/gur(

kg ⋅ m

−3

) ) ) )

T K

ρexp ± 2σ est

ρexp − ρcalc kg ⋅ m−3

−3

kg ⋅ m

323.15 829.10 ± 0.50 333.15 822.00 ± 0.50 343.15 815.50 ± 0.50

−0.67 −0.46 0.35

Ref. (Symbol in Fig. 1)

88-bag/gur( ) 88-bag/gur( ) 88-bag/gur( )

ρ

ρ

293.15 293.15 303.15 313.15

ρexp − ρcalc

−3

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

290.00 293.15 298.15

Landolt-Börnstein New Series IV/8G

ρ ± σ fit kg ⋅ m−3 854.02 ± 1.42 851.71 ± 1.24 848.06 ± 0.98

T K

300.00 310.00 320.00

ρ ± σ fit kg ⋅ m−3 846.70 ± 0.89 839.39 ± 0.54 832.08 ± 0.38

T K

330.00 340.00 350.00

ρ ± σ fit kg ⋅ m−3 824.77 ± 0.42 817.45 ± 0.63 810.14 ± 1.00

2.2.3 Alcohols of General Formula CnH2n-4O

295

2.2.3 Alcohols of General Formula CnH2n-4O 1-Hexen-5-yn-3-ol

[1573-66-6]

C6H8O

MW = 96.13

619

C6H8O

MW = 96.13

620

C7H10O

MW = 110.16

621

C7H10O

MW = 110.16

622

C8H12O

MW = 124.18

623

C8H12O

MW = 124.18

624

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

919.0 ± 0.7

63-lab

(RS)-1-Hexen-5-yn-3-ol

[126110-03-0]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

915.5 ± 1.0

65-alb/bry

2-Hepten-6-yn-4-ol

[500025-44-5]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

925.6 ± 0.7

63-lab

3-Methyl-1-hexen-5-yn-3-ol

[1573-67-7]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

−3

kg ⋅ m

906.6 ± 1.0

65-alb/bry

4-Methyl-1,2,6-heptatrien-4-ol

[90198-78-0]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

294.15

Ref.

−3

kg ⋅ m

900.6 ± 2.0

62-ber/leg

6-Methyl-1,3,4-heptatrien-6-ol

[500025-52-5]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

882.5 ± 0.7

Landolt-Börnstein New Series IV/8G

63-lab

296

2.2.3 Alcohols of General Formula CnH2n-4O

4-Ethyl-1,2,6-heptatrien-4-ol

[90611-15-7]

C9H14O

MW = 138.21

625

C9H14O

MW = 138.21

626

C9H14O

MW = 138.21

627

C 10H16O

MW = 152.2

628

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

895.4 ± 2.0

62-ber/leg

6-Methyl-1,3,4-octatrien-6-ol

[500025-51-4]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

885.5 ± 0.7

63-lab

2,4,5-Nonatrien-7-ol

[500025-50-3]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

891.8 ± 0.7

63-lab

3,7-Dimethyl-6-octen-1-yn-3-ol

[29171-20-8]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 5.4842 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.6817 · 10−1 (combined temperature ranges, unweighted). Coefficient A B

T = 293.15 to 343.15 K ρ = A + BT + CT 2 + DT 3 + … 1.12321 · 103 −8.36474 · 10−1

Table 2. Experimental values with uncertainties and deviation from calculated values. T K

293.15 303.15 313.15 323.15 333.15 343.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

878.60 ± 1.00 869.50 ± 1.00 861.20 ± 1.00 852.40 ± 1.00 843.80 ± 1.00 837.00 ± 1.00

0.60 −0.13 −0.07 −0.50 −0.74 0.83

Ref. (Symbol in Fig. 1) 85-bel/ber( 85-bel/ber( 85-bel/ber( 85-bel/ber( 85-bel/ber( 85-bel/ber(

) ) ) ) ) )

T K

293.15 303.15 313.15 323.15 333.15 343.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

878.60 ± 1.00 869.50 ± 1.00 861.20 ± 1.00 852.40 ± 1.00 843.80 ± 1.00 837.00 ± 1.00

0.60 −0.13 −0.07 −0.50 −0.74 0.83

Ref. (Symbol in Fig. 1) 88-bag/gur( 88-bag/gur( 88-bag/gur( 88-bag/gur( 88-bag/gur( 88-bag/gur(

) ) ) ) ) ) cont.

Landolt-Börnstein New Series IV/8G

2.2.3 Alcohols of General Formula CnH2n-4O

297

ρ

ρ

3,7-Dimethyl-6-octen-1-yn-3-ol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ).

ρ ± σ fit kg ⋅ m−3

T K

880.63 ± 1.26 878.00 ± 1.21 873.81 ± 1.13

290.00 293.15 298.15

ρ ± σ fit kg ⋅ m−3

T K

872.27 ± 1.10 863.90 ± 0.94 855.54 ± 0.86

300.00 310.00 320.00

3-Methyl-2-nonen-4-yn-6-ol

[500025-47-8]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

kg ⋅ m−3

881.3 ± 0.6

Landolt-Börnstein New Series IV/8G

63-lab

T K

330.00 340.00 350.00

C10H16O

ρ ± σ fit kg ⋅ m−3 847.17 ± 0.91 838.81 ± 1.18 830.44 ± 1.72

MW = 152.24

629

298

2.2.3 Alcohols of General Formula CnH2n-4O

4-(1-Methylethyl)-1,2,6-heptatrien-4-ol

[91055-94-6]

C 10H16O

MW = 152.24

630

C10H16O

MW = 152.24

631

C11H18O

MW = 166.26

632

C11H18O

MW = 166.26

633

C11H18O

MW = 166.26

634

C12H20O

MW = 180.29

635

Table 1. Experimental value with uncertainty. T K 295.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

885.1 ± 2.0

62-ber/leg

4-Propyl-1,2,6-heptatrien-4-ol

[91055-95-7]

Table 1. Experimental value with uncertainty. T K 294.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

882.1 ± 2.0

62-ber/leg

3-Ethenyl-1-nonyn-4-ol

[900002-83-7]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

879.0 ± 2.0

65-mig/mig

5-Methyl-2,5,6-decatrien-4-ol

[14129-53-4]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

871.5 ± 1.0

66-per/bal

3-(Methylethenyl)-3,4-octadien-2-ol

[14129-70-5]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

874.3 ± 1.0

66-per/bal

2-Methyl-3-(1-methylethenyl)3,4-octadien-2-ol

[14270-82-7]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

855.5 ± 1.0

66-per/bal

Landolt-Börnstein New Series IV/8G

2.2.3 Alcohols of General Formula CnH2n-4O 2,7-Dimethyl-3-(1-methylethenyl)3,4-octadien-2-ol

[14270-85-0]

299

C13H22O

MW = 194.32

636

C 13H22O

MW = 194.32

637

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

−3

kg ⋅ m

855.8 ± 1.0

66-per/bal

5-Ethyl-9-methyl-2,5,6-decatrien-4-ol

[14129-71-6]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

867.1 ± 1.0

Landolt-Börnstein New Series IV/8G

66-per/bal

2.2.4 Alcohols of General Formula CnH2n-6O

301

2.2.4 Alcohols of General Formula CnH2n-6O 1,6-Heptadiyn-4-ol

[21972-06-5]

C7H8O

MW = 108.14

638

C8H10O

MW = 122.17

639

C8H10O

MW = 122.17

640

C9H12O

MW = 136.19

641

C9H12O

MW = 136.19

642

C11H16O

MW = 164.25

643

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

−3

kg ⋅ m

967.2 ± 1.0

63-lab

4-Methyl-1,6-heptadiyn-4-ol

[41005-07-6]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

kg ⋅ m−3

959.5 ± 1.0

63-lab

1,7-Octadien-5-yn-3-ol

[1573-68-8]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

kg ⋅ m−3

922.5 ± 1.0

65-alb/bry

3-Methyl-1,7-octadien-5-yn-3-ol

[1573-69-9]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

910.5 ± 1.0

65-alb/bry

2-Methyl-3,5-octadiyn-2-ol

[500025-48-9]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

870.0 ± 1.0

63-lab

2-Methyl-3,5-decadiyn-2-ol

[500025-49-0]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

897.3 ± 1.0

Landolt-Börnstein New Series IV/8G

63-lab

3.1.1 Alkanediols, C1 - C6

303

3 Tabulated Data on Density - Diols 3.1 Alkanediols 3.1.1 Alkanediols C1 - C6 1,2-Ethanediol

[107-21-1]

C2H6O2

MW = 62.07

644

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 6.0901 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.3696 · 10−1 (combined temperature ranges, unweighted). Coefficient A B C D

T = 250.25 to 513.15 K ρ = A + BT + CT 2 + DT 3 + … 1.31971 · 103 −8.26843 · 10−1 8.03242 · 10−4 −1.30719 · 10−6

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 289.95 1118.00 ± 2.00 2.37 1893-ram/shi-31) 343.15 1077.40 ± 0.60 −0.34 319.25 1091.20 ± 2.00 −3.87 1893-ram/shi-31) 273.15 1126.00 ± 1.00 −1.15 351.35 1068.00 ± 2.00 −3.66 1893-ram/shi-31) 293.15 1113.00 ± 1.00 −0.42 405.05 1029.70 ± 2.00 −0.01 1893-ram/shi-3(✕ ) 313.15 1100.00 ± 1.00 0.59 292.45 1113.40 ± 1.00 −0.50 1895-eyk1) 333.15 1086.00 ± 1.00 0.94 411.95 1023.00 ± 2.00 −1.02 1895-eyk(✕ ) 353.15 1071.00 ± 1.00 0.69 293.15 1112.72 ± 1.00 −0.70 30-bin/for1) 373.15 1056.00 ± 1.00 0.90 303.15 1105.58 ± 1.00 −0.87 30-bin/for1) 393.15 1041.00 ± 1.00 1.64 313.15 1098.78 ± 1.00 −0.63 30-bin/for1) 413.15 1024.00 ± 1.00 0.98 1) 333.15 1084.13 ± 1.00 −0.93 30-bin/for 433.15 1007.00 ± 1.00 0.97 353.15 1069.63 ± 1.00 −0.68 30-bin/for(✕ ) 453.15 989.20 ± 1.00 0.87 371.15 1054.52 ± 1.00 −2.12 30-bin/for(✕ ) 473.15 970.80 ± 1.50 0.95 393.15 1037.45 ± 1.00 −1.91 30-bin/for(✕ ) 493.15 950.30 ± 1.50 −0.22 298.15 1109.90 ± 0.60 −0.04 31-smy/wal1) 513.15 930.40 ± 1.50 0.11 323.15 1092.30 ± 0.60 0.02 31-smy/wal(✕ ) 533.15 910.30 ± 1.50 1.20 273.15 1127.60 ± 0.20 0.45 553.15 889.20 ± 1.50 2.33 35-tim/hen(∆) 288.15 1117.07 ± 0.20 0.20 250.25 1140.70 ± 0.60 −1.91 35-tim/hen(∆) 303.15 1106.61 ± 0.20 0.16 366.25 1067.80 ± 0.60 7.40 35-tim/hen(∆) 293.15 1113.10 ± 0.60 −0.32 53-dan/fad1) 293.10 1113.96 ± 0.50 0.51 333.15 1085.10 ± 0.60 0.04 53-dan/fad(✕ ) 298.10 1110.28 ± 0.50 0.30 1) 293.15 1113.10 ± 0.60 −0.32 57-ket/van 303.10 1106.72 ± 0.50 0.23 318.15 1095.50 ± 0.60 −0.36 57-ket/van(✕ ) 308.10 1103.06 ± 0.50 0.08 1)

Ref. (Symbol in Fig. 1) 57-ket/van(✕ ) 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow1) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow1) 58-cos/bow1) 59-kom/ros(✕ ) 59-kom/ros1) 75-khi/gri1) 75-khi/gri1) 75-khi/gri1) 75-khi/gri1)

Not included in Fig. 1.

cont. Landolt-Börnstein New Series IV/8G

304

3.1.1 Alkanediols, C1 - C6

1,2-Ethanediol (cont.) Table 2. (cont.) ρexp ± 2σ est T K kg ⋅ m−3 313.10 1099.58 ± 0.50 318.10 1095.99 ± 0.50 323.10 1092.24 ± 0.50 293.15 1113.50 ± 0.25 298.00 1094.00 ± 1.00 318.00 1109.00 ± 1.00 338.00 1080.00 ± 1.00 358.00 1065.00 ± 1.00 298.15 1109.82 ± 0.20 303.15 1105.90 ± 0.60 313.30 1099.90 ± 0.60 336.00 1083.80 ± 0.60 354.40 1069.80 ± 0.70 363.15 1063.70 ± 0.70 373.15 1055.90 ± 0.70

kg ⋅ m−3

0.13 0.10 −0.08 0.08 −16.05 13.04 −1.53 −1.67 −0.12 −0.55 0.60 0.81 0.42 0.93 0.80

T K 75-khi/gri(✕ ) 393.40 75-khi/gri(✕ ) 422.80 75-khi/gri(✕ ) 283.15 81-joo/arl(∇) 293.15 84-idr/fre1) 303.15 84-idr/fre1) 288.15 84-idr/fre(✕ ) 298.15 84-idr/fre(✕ ) 303.15 88-dou/pal( ) 308.15 89-taw/tej1) 293.15 89-taw/tej1) 273.15 89-taw/tej(✕ ) 293.15 89-taw/tej(✕ ) 313.15 89-taw/tej(✕ ) 333.15 89-taw/tej(✕ )

Ref. (Symbol in Fig. 1)

ρexp ± 2σ est −3

kg ⋅ m

1040.80 ± 0.70 1015.80 ± 0.80 1119.29 ± 0.50 1112.02 ± 0.50 1105.82 ± 0.50 1116.96 ± 0.20 1109.99 ± 0.20 1106.49 ± 0.20 1102.96 ± 0.20 1113.47 ± 0.30 1126.90 ± 0.40 1113.10 ± 0.40 1099.00 ± 0.40 1084.70 ± 0.40

ρexp − ρcalc kg ⋅ m−3

1.64 0.89 −1.02 −1.40 −0.63 0.09 0.05 0.04 0.02 0.05 −0.25 −0.32 −0.41 −0.36

Ref. (Symbol in Fig. 1) 89-taw/tej(✕ ) 89-taw/tej(✕ ) 90-lee/hon(✕ ) 90-lee/hon1) 90-lee/hon1) 91-dou/pal( ) 91-dou/pal( ) 91-dou/pal( ) 91-dou/pal( ) 93-chi/pro(◆) 93-kum/moc(✕ ) 93-kum/moc(✕ ) 93-kum/moc(✕ ) 93-kum/moc(✕ )

Not included in Fig. 1.

ρ

ρ

1)

ρexp − ρcalc

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont.

Landolt-Börnstein New Series IV/8G

3.1.1 Alkanediols, C1 - C6

305

Further references: [1859-wur, 1864-lan, 1884-gla, 1884-per, 01-def-1, 05-dun, 06-wal-1, 07-wal-4, 09-sch-2, 14-low, 18-kar, 19-eyk, 25-rii/soe, 26-tay/rin, 27-kai/mel, 29-ber/reu, 32-bri-2, 35-sch/sta, 36-rom, 37-ewe, 37-gib/kin, 37-mou/dod, 37-puk, 41-gib/loe, 43-ish/kat, 44-ira, 48-lad/smi, 48-wei, 52-cur/joh, 53-ish/kat, 55-fog/hix, 56-koi/han, 57-cru/jos, 60-rab/mur, 61-lut/obu, 62-mel, 65-por/pli, 66-gar/kom, 66-koz/rab, 67-dav/fin, 67-sho/ata, 68-ano, 68-naz/tsy, 69-ada, 70-kun/cha, 70-paz/paz, 70-ras/gaz, 72-gla/gha, 74-jim/paz, 74-wol/ska, 75-esp/man, 77-zhu/zhu-2, 78-fro/ers-1, 78-mus/kan, 79-jim/paz, 79-sah/hay, 79-sin/siv, 82-diz/mar, 82-man/les, 85-zhu, 91-fen/wan, 98-pal/sha].

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K 250.00 260.00 270.00 280.00 290.00 293.15 298.15 300.00 310.00 320.00

ρ ± σ fit kg ⋅ m−3

ρ ± σ fit kg ⋅ m−3

T K

1142.78 ± 0.45 1136.05 ± 0.40 1129.29 ± 0.38 1122.47 ± 0.39 1115.60 ± 0.41 1113.42 ± 0.42 1109.94 ± 0.44 1108.65 ± 0.45 1101.64 ± 0.49 1094.54 ± 0.53

T K

1087.35 ± 0.58 1080.06 ± 0.63 1072.67 ± 0.69 1065.16 ± 0.75 1057.53 ± 0.81 1049.77 ± 0.88 1041.87 ± 0.95 1033.83 ± 1.03 1025.64 ± 1.11 1017.28 ± 1.19

330.00 340.00 350.00 360.00 370.00 380.00 390.00 400.00 410.00 420.00

1,2-Propanediol

[57-55-6]

430.00 440.00 450.00 460.00 470.00 480.00 490.00 500.00 510.00 520.00

C3H8O2

ρ ± σ fit kg ⋅ m−3 1008.76 ± 1.28 1000.05 ± 1.37 991.17 ± 1.47 982.09 ± 1.58 972.81 ± 1.69 963.33 ± 1.82 953.63 ± 1.97 943.70 ± 2.14 933.54 ± 2.33 923.15 ± 2.55

MW = 76.1

645

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 3.0002 · 10−1 (combined temperature ranges, weighted), σc,uw = 4.9012 · 10−2 (combined temperature ranges, unweighted). Coefficient A B

T = 273.15 to 323.15 K ρ = A + BT + CT 2 + DT 3 + … 1.25088 · 103 −7.32395 · 10−1

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) ⋅ kg m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 298.15 1032.80 ± 0.80 0.28 31-smy/wal1) 296.15 1035.40 ± 0.50 1.42 323.15 1013.80 ± 0.80 −0.41 31-smy/wal(✕ ) 278.15 1047.20 ± 0.60 0.03 293.15 1038.10 ± 1.00 1.92 51-mac/tho1) 283.15 1043.50 ± 0.60 −0.00 308.15 1025.10 ± 1.00 −0.09 51-mac/tho(✕ ) 288.15 1039.90 ± 0.60 0.06 273.15 1050.60 ± 1.00 −0.23 51-van-1(✕ ) 293.15 1036.30 ± 0.60 0.12 293.15 1037.60 ± 1.00 1.42 51-van-11) 298.15 1032.60 ± 0.60 0.08 273.15 1050.81 ± 0.40 −0.02 303.15 1028.90 ± 0.60 0.04 55-tim/hen(∆) 288.15 1040.01 ± 0.40 0.17 308.15 1025.30 ± 0.60 0.11 55-tim/hen(∆) 303.15 1029.08 ± 0.40 0.22 313.15 1021.70 ± 0.60 0.17 55-tim/hen(∆) 293.15 1036.20 ± 0.40 0.02 57-ano( ) 318.15 1018.10 ± 0.80 0.23 293.15 1036.10 ± 0.50 −0.08 298.15 1032.00 ± 0.40 −0.52 62-mel(∇) 293.15 1036.40 ± 0.50 0.22 62-mel(∇)

1)

Not included in Fig. 1.

Landolt-Börnstein New Series IV/8G

Ref. (Symbol in Fig. 1) 62-mel1) 70-kun/cha(◆) 70-kun/cha(◆) 70-kun/cha(◆) 70-kun/cha1) 70-kun/cha(◆) 70-kun/cha(◆) 70-kun/cha(◆) 70-kun/cha(◆) 70-kun/cha(◆) 85-les/eic( )

cont.

306

3.1.1 Alkanediols, C1 - C6

1,2-Propanediol (cont.)

ρ

ρ

Further references: [1857-wur-1, 1859-wur, 1879-bel, 1882-zan, 1890-gar, 27-tro/luk, 32-bri-2, 35-sch/sta, 36-dup-1, 37-puk, 46-puc/wis, 50-cle/mac, 52-cur/joh, 53-ano-5, 55-ano-2, 61-sch-3, 62-deg/lad, 65-wei/lan, 66-mil-1, 68-ano, 70-gar/kom, 73-gar/paz, 74-wol/ska, 78-mus/kan, 82-man/les].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00

ρ ± σ fit kg ⋅ m−3 1053.14 ± 0.86 1045.81 ± 0.64 1038.49 ± 0.50

T K

293.15 298.15 300.00

ρ ± σ fit kg ⋅ m−3 1036.18 ± 0.48 1032.52 ± 0.49 1031.16 ± 0.50

T K

310.00 320.00 330.00

ρ ± σ fit kg ⋅ m−3 1023.84 ± 0.64 1016.52 ± 0.96 1009.19 ± 1.47

Landolt-Börnstein New Series IV/8G

3.1.1 Alkanediols, C1 - C6 1,3-Propanediol

[504-63-2]

307

C3H8O2

MW = 76.1

646

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 8.3438 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.6142 · 10−1 (combined temperature ranges, unweighted). T = 273.15 to 343.15 K ρ = A + BT + CT 2 + DT 3 + … 1.13576 · 103 2.29954 · 10−2 −1.03995 · 10−3

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 273.15 1063.40 ± 2.00 −1.05 1874-reb-2(✕ ) 343.15 1021.80 ± 0.60 0.60 292.15 1053.00 ± 2.00 −0.72 1874-reb-21) 293.15 1053.80 ± 0.50 0.67 298.15 1050.30 ± 0.80 0.13 31-smy/wal(✕ ) 293.15 1052.90 ± 0.50 −0.23 323.15 1034.40 ± 0.80 −0.20 31-smy/wal(✕ ) 298.15 1049.00 ± 2.00 −1.17 293.15 1052.80 ± 0.60 −0.33 32-bri-2(✕ ) 323.15 1033.00 ± 2.00 −1.60 293.15 1053.80 ± 0.50 0.67 373.15 1003.00 ± 2.00 3.46 35-sch/sta(∆) 293.15 1053.60 ± 0.60 0.47 52-cur/joh(◆) 293.15 1053.70 ± 0.40 0.57 293.15 1052.90 ± 0.40 −0.23 53-ano-6( ) 303.15 1047.44 ± 0.40 0.28 293.15 1053.30 ± 0.60 0.17 57-ket/van(✕ ) 313.15 1041.10 ± 0.40 0.12 318.15 1037.80 ± 0.60 −0.02 57-ket/van(✕ )

1)

Ref. (Symbol in Fig. 1) 57-ket/van(✕ ) 62-mel(∇) 62-mel(∇) 80-bru1) 80-bru(✕ ) 80-bru1) 88-cze/zyw( ) 88-cze/zyw( ) 88-cze/zyw( )

Not included in Fig. 1.

Further references: [1874-reb-1, 1882-zan, 18-kar, 26-ray, 36-sto/rou, 50-cle/mac, 59-ale, 72-rak/isa, 74-paz/rom, 74-rak/mel, 74-rak/zlo, 75-nak/kom, 78-mus/kan].

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15

ρ ± σ fit kg ⋅ m−3 1066.16 ± 1.82 1060.67 ± 1.16 1054.97 ± 0.73 1053.13 ± 0.64

T K

298.15 300.00 310.00 320.00

ρ ± σ fit kg ⋅ m−3 1050.17 ± 0.56 1049.07 ± 0.55 1042.95 ± 0.56 1036.63 ± 0.72

T K

330.00 340.00 350.00

ρ ± σ fit kg ⋅ m−3 1030.10 ± 1.04 1023.36 ± 1.56 1016.42 ± 2.29

cont.

Landolt-Börnstein New Series IV/8G

308

3.1.1 Alkanediols, C1 - C6

ρ

ρ

1,3-Propanediol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

R-(-)-1,2-Propanediol

[4254-14-2]

C3H8O2

MW = 76.1

647

C3H8O2

MW = 76.1

648

Table 1. Experimental values with uncertainties. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 18-abd/eic 1004.3 ± 3.0 299.15 56-pri/osg 1025.3 ± 3.0

(S)-(+)-1,2-Propanediol

[4254-15-3]

Table 1. Experimental values with uncertainties. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 48-bae/fis 1040.0 ± 3.0 295.15 62-kuh/kuh 1041.0 ± 3.0

Landolt-Börnstein New Series IV/8G

3.1.1 Alkanediols, C1 - C6 1,2-Butanediol

[584-03-2]

309

C4H10O2

MW = 90.12

649

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 1.1759 (combined temperature ranges, weighted), σc,uw = 2.4556 · 10−1 (combined temperature ranges, unweighted). T = 293.15 to 454.70 K ρ = A + BT + CT 2 + DT 3 + … 1.09605 · 103 2.45483 · 10−2 −1.17159 · 10−3

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc Ref. (Symbol ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 293.15 1004.60 ± 2.00 2.04 37-tis(✕ ) 318.80 984.80 ± 0.50 −0.00 92-sun/dig( ) 293.15 1001.00 ± 2.00 −1.56 37-tis/chu(✕ ) 337.70 970.00 ± 0.50 −0.73 92-sun/dig( ) 293.15 1002.40 ± 1.00 −0.16 50-cle/mac(◆) 357.70 954.70 ± 0.50 −0.23 92-sun/dig( ) 293.15 1002.40 ± 1.00 −0.16 370.90 943.70 ± 0.50 −0.28 92-sun/dig( ) 62-mel(∇) 293.15 1002.80 ± 1.00 0.24 393.90 923.90 ± 0.50 −0.04 92-sun/dig( ) 65-wei/lan(∆) 293.15 1003.47 ± 0.40 0.91 88-cze/zyw( ) 413.50 907.40 ± 0.50 1.52 92-sun/dig( ) 303.15 995.44 ± 0.40 −0.38 88-cze/zyw( ) 434.60 886.50 ± 0.50 1.07 92-sun/dig( ) 313.15 987.87 ± 0.40 −0.98 88-cze/zyw( ) 454.70 863.40 ± 0.50 −1.58 92-sun/dig( ) 301.80 997.10 ± 0.50 0.35 92-sun/dig( )

Further references: [1886-hen, 73-sza/mys].

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

290.00 293.15 298.15 300.00 310.00 320.00 330.00

ρ ± σ fit kg ⋅ m−3 1004.64 ± 1.23 1002.56 ± 1.13 999.22 ± 0.98 997.97 ± 0.93 991.07 ± 0.71 983.93 ± 0.54 976.57 ± 0.44

T K

340.00 350.00 360.00 370.00 380.00 390.00 400.00

ρ ± σ fit kg ⋅ m−3 968.96 ± 0.38 961.12 ± 0.36 953.05 ± 0.36 944.74 ± 0.38 936.20 ± 0.42 927.43 ± 0.46 918.42 ± 0.52

T K

410.00 420.00 430.00 440.00 450.00 460.00

ρ ± σ fit kg ⋅ m−3 909.17 ± 0.58 899.69 ± 0.65 889.98 ± 0.72 880.03 ± 0.78 869.85 ± 0.84 859.43 ± 0.89

cont.

Landolt-Börnstein New Series IV/8G

310

3.1.1 Alkanediols, C1 - C6

ρ

ρ

1,2-Butanediol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

(RS)-1,2-Butanediol

[26171-83-5]

C4H10O2

MW = 90.12

650

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 4.4743 · 10−1 (combined temperature ranges, weighted), σc,uw = 2.2372 · 10−1 (combined temperature ranges, unweighted). Coefficient A B C

T = 323.14 to 448.11 K ρ = A + BT + CT 2 + DT 3 + … 1.11932 · 103 −1.05834 · 10−1 −1.01373 · 10−3

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc Ref. (Symbol ρexp ± 2σ est ρexp ± 2σ est T T −3 3 −3 − in Fig. 1) in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 323.14 979.00 ± 0.50 −0.27 96-ste/chi( ) 398.12 916.00 ± 0.50 −0.51 96-ste/chi( ) 348.14 959.80 ± 0.50 0.19 96-ste/chi( ) 423.11 892.60 ± 0.50 −0.46 96-ste/chi( ) 373.12 939.40 ± 0.50 0.70 96-ste/chi( ) 448.11 868.70 ± 0.50 0.36 96-ste/chi( ) cont.

Landolt-Börnstein New Series IV/8G

311

ρ

ρ

3.1.1 Alkanediols, C1 - C6

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

320.00 330.00 340.00 350.00 360.00

Landolt-Börnstein New Series IV/8G

ρ ± σ fit kg ⋅ m−3 981.65 ± 0.78 974.00 ± 0.69 966.15 ± 0.62 958.10 ± 0.57 949.84 ± 0.54

T K

370.00 380.00 390.00 400.00 410.00

ρ ± σ fit kg ⋅ m−3 941.38 ± 0.51 932.72 ± 0.50 923.86 ± 0.48 914.79 ± 0.47 905.52 ± 0.48

T K

420.00 430.00 440.00 450.00 460.00

ρ ± σ fit kg ⋅ m−3 896.05 ± 0.51 886.38 ± 0.58 876.50 ± 0.71 866.42 ± 0.89 856.13 ± 1.13

312

3.1.1 Alkanediols, C1 - C6

1,3-Butanediol

[107-88-0]

C4H10O2

MW = 90.12

651

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 8.4552 · 10−1 (combined temperature ranges, weighted), σc,uw = 2.2006 · 10−1 (combined temperature ranges, unweighted). T = 293.15 to 458.90 K ρ = A + BT + CT 2 + DT 3 + … 1.09606 · 103 −8.02845 · 10−3 −1.03339 · 10−3

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 298.15 1000.20 ± 1.00 −1.60 323.10 986.10 ± 0.60 0.52 48-adk/bil(∇) 293.15 1003.50 ± 0.60 −1.40 342.90 970.80 ± 0.60 −1.00 62-mel(∆) 293.15 1002.00 ± 1.00 −2.90 62-mel1) 363.00 957.20 ± 0.60 0.23 293.15 1003.70 ± 0.60 −1.20 383.20 941.50 ± 0.60 0.27 62-mel(∆) 293.15 1005.30 ± 0.70 0.40 400.90 927.00 ± 0.60 0.25 62-mel(∆) 293.15 1005.79 ± 0.40 0.89 88-cze/zyw( ) 420.30 910.40 ± 0.60 0.27 303.15 999.04 ± 0.40 0.39 88-cze/zyw( ) 439.60 893.10 ± 0.60 0.27 313.15 992.39 ± 0.40 0.19 88-cze/zyw( ) 458.90 874.80 ± 0.60 0.05 302.40 1000.60 ± 0.60 1.47 92-sun/dig( )

1)

Ref. (Symbol in Fig. 1)

) ) ) ) ) ) ) )

92-sun/dig( 92-sun/dig( 92-sun/dig( 92-sun/dig( 92-sun/dig( 92-sun/dig( 92-sun/dig( 92-sun/dig(

Not included in Fig. 1.

Further references: [29-ber/mie, 35-sch/sta, 37-tis/chu, 43-gre/kel, 48-bou/nic, 48-mic/hop, 50-cle/mac, 52-cur/joh, 54-ros, 55-ser, 56-far/she, 67-pis/gas, 72-rak/isa, 74-rak/mak, 74-rak/mel, 74-wol/ska, 78-mus/kan, 82-man/les].

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

290.00 293.15 298.15 300.00 310.00 320.00 330.00

ρ ± σ fit kg ⋅ m−3 1006.82 ± 0.72 1004.90 ± 0.69 1001.80 ± 0.66 1000.64 ± 0.65 994.26 ± 0.60 987.67 ± 0.57 980.87 ± 0.55

T K

340.00 350.00 360.00 370.00 380.00 390.00 400.00

ρ ± σ fit kg ⋅ m−3 973.87 ± 0.54 966.66 ± 0.54 959.24 ± 0.54 951.61 ± 0.55 943.78 ± 0.56 935.75 ± 0.58 927.50 ± 0.60

T K

410.00 420.00 430.00 440.00 450.00 460.00 470.00

ρ ± σ fit kg ⋅ m−3 919.05 ± 0.63 910.39 ± 0.67 901.53 ± 0.73 892.46 ± 0.81 883.18 ± 0.90 873.70 ± 1.01 864.01 ± 1.14

cont. Landolt-Börnstein New Series IV/8G

313

ρ

ρ

3.1.1 Alkanediols, C1 - C6

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

(RS)-1,3-Butanediol

[18826-95-4]

C4H10O2

MW = 90.12

652

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 4.2923 · 10−1 (combined temperature ranges, weighted), σc,uw = 2.1462 · 10−1 (combined temperature ranges, unweighted). Coefficient A B C

T = 323.14 to 448.11 K ρ = A + BT + CT 2 + DT 3 + … 1.07840 · 103 8.73975 · 10−2 −1.18509 · 10−3

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc Ref. (Symbol ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 323.14 982.80 ± 0.50 −0.10 96-ste/chi( ) 448.11 880.00 ± 0.50 0.40 96-ste/chi( ) 348.13 965.10 ± 0.50 −0.10 96-ste/chi( ) 672.80 391.30 ± 0.00 −209.46 96-ste/chi1) 373.12 946.50 ± 0.50 0.48 96-ste/chi( ) 674.50 348.90 ± 0.00 −249.29 96-ste/chi1) 398.12 925.50 ± 0.50 0.14 96-ste/chi( ) 675.40 316.00 ± 0.00 −280.83 96-ste/chi1) 423.11 902.40 ± 0.50 −0.82 96-ste/chi( )

1)

Not included in Fig. 1.

Landolt-Börnstein New Series IV/8G

cont.

314

3.1.1 Alkanediols, C1 - C6

ρ

ρ

(RS)-1,3-Butanediol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

320.00 330.00 340.00 350.00 360.00

ρ ± σ fit kg ⋅ m−3 985.02 ± 0.78 978.19 ± 0.69 971.12 ± 0.62 963.82 ± 0.57 956.28 ± 0.54

T K

370.00 380.00 390.00 400.00 410.00

ρ ± σ fit kg ⋅ m−3 948.50 ± 0.51 940.49 ± 0.50 932.23 ± 0.48 923.75 ± 0.47 915.02 ± 0.48

T K

420.00 430.00 440.00 450.00 460.00

ρ ± σ fit kg ⋅ m−3 906.06 ± 0.51 896.86 ± 0.58 887.42 ± 0.71 877.75 ± 0.89 867.84 ± 1.13

Landolt-Börnstein New Series IV/8G

3.1.1 Alkanediols, C1 - C6 1,4-Butanediol

[110-63-4]

315

C4H10O2

MW = 90.12

653

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 1.0892 (combined temperature ranges, weighted), σc,uw = 2.6052 · 10−1 (combined temperature ranges, unweighted). T = 293.15 to 493.15 K ρ = A + BT + CT 2 + DT 3 + … 1.12256 · 103 −1.72321 · 10−1 −5.89027 · 10−4 −1.76600 · 10−7

Coefficient A B C D

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 293.15 1017.10 ± 0.80 0.13 29-kir/ric(✕ ) 493.15 874.60 ± 1.00 1.45 293.15 1016.00 ± 0.60 −0.97 48-bou/nic(∇) 293.15 1016.22 ± 0.40 −0.75 293.15 1017.30 ± 1.00 0.33 57-ket/van1) 303.15 1010.11 ± 0.40 −1.16 318.15 1001.80 ± 1.00 −0.63 57-ket/van(✕ ) 313.15 1004.15 ± 0.40 −1.26 343.15 985.90 ± 1.00 −1.03 57-ket/van(✕ ) 303.30 1011.40 ± 0.60 0.22 293.15 1017.10 ± 0.70 0.13 62-mel(◆) 322.10 999.00 ± 0.60 −1.04 293.15 1016.00 ± 0.60 −0.97 62-mel(◆) 343.00 986.40 ± 0.60 −0.63 293.15 1018.50 ± 0.60 1.53 62-mel(◆) 363.60 973.30 ± 0.60 −0.24 298.15 1015.40 ± 1.00 1.26 62-mel(◆) 384.80 959.30 ± 0.60 0.33 298.15 1015.40 ± 0.60 1.26 66-fre/hor( ) 402.20 946.50 ± 0.60 0.02 295.15 1017.80 ± 1.00 1.96 78-apa/ker-2(✕ ) 423.30 930.50 ± 0.60 −0.18 358.16 980.20 ± 1.00 3.03 78-apa/ker-2(✕ ) 442.30 915.60 ± 0.60 −0.23 451.11 913.00 ± 1.00 4.26 78-apa/ker-21) 460.30 899.00 ± 0.60 −2.22

1)

Ref. (Symbol in Fig. 1) 78-apa/ker-2(✕ ) 88-cze/zyw( ) 88-cze/zyw( ) 88-cze/zyw( ) 92-sun/dig(∆) 92-sun/dig(∆) 92-sun/dig(∆) 92-sun/dig(∆) 92-sun/dig(∆) 92-sun/dig(∆) 92-sun/dig(∆) 92-sun/dig(∆) 92-sun/dig(∆)

Not included in Fig. 1.

Further references: [1890-dek, 01-ham, 32-hun, 50-cle/mac, 52-cur/joh, 54-ros, 60-kun/sak, 63-shu/bar, 66-mya/pya, 68-naz/tsy, 70-are/tav, 78-mus/kan, 82-man/les].

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

290.00 293.15 298.15 300.00 310.00 320.00 330.00 340.00

ρ ± σ fit kg ⋅ m−3 1018.74 ± 0.69 1016.97 ± 0.70 1014.14 ± 0.71 1013.08 ± 0.72 1007.27 ± 0.76 1001.31 ± 0.78 995.20 ± 0.79 988.94 ± 0.78

T K

350.00 360.00 370.00 380.00 390.00 400.00 410.00 420.00

ρ ± σ fit kg ⋅ m−3 982.52 ± 0.76 975.95 ± 0.73 969.22 ± 0.69 962.33 ± 0.66 955.29 ± 0.63 948.08 ± 0.61 940.72 ± 0.61 933.20 ± 0.61

T K

430.00 440.00 450.00 460.00 470.00 480.00 490.00 500.00

ρ ± σ fit kg ⋅ m−3 925.51 ± 0.63 917.66 ± 0.66 909.64 ± 0.71 901.46 ± 0.80 893.12 ± 0.94 884.60 ± 1.14 875.92 ± 1.40 867.07 ± 1.74 cont.

Landolt-Börnstein New Series IV/8G

316

3.1.1 Alkanediols, C1 - C6

ρ

ρ

1,4-Butanediol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

2,3-Butanediol (isomer not specified)

[513-85-9]

C4H10O2

MW = 90.12

654

Table 1. Fit with estimated B coefficient for 5 accepted points. Deviation σw = 0.509. Coefficient ρ = A + BT A 1238.27 B −0.800

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. ρexp − ρcalc Ref. ρexp ± 2σ est ρexp ± 2σ est T T kg ⋅ m−3 kg ⋅ m−3 K K kg ⋅ m−3 kg ⋅ m−3 293.15 1007.6 ± 3.0 3.85 62-mel1) 293.15 1005.0 ± 2.0 1.25 65-wei/lan 293.15 1003.3 ± 1.0 64-mys/zie 293.15 1003.3 ± 1.0 35-sch/sta −0.45 −0.45 298.15 1000.3 ± 1.0 0.55 64-mys/zie 298.15 999.8 ± 1.0 0.05 46-cle-1 1)

Not included in calculation of linear coefficients.

cont.

Landolt-Börnstein New Series IV/8G

3.1.1 Alkanediols, C1 - C6

317

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 290.00 1006.3 ± 1.1 293.15 1003.8 ± 1.0 298.15 999.8 ± 1.0 D-(-)-2,3-Butanediol

[24347-58-8]

C4H10O2

MW = 90.12

655

C4H10O2

MW = 90.12

656

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 46-kno/sch 987.2 ± 0.5 dl-2,3-Butanediol

[6982-25-8]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 7.3545 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.9800 · 10−1 (combined temperature ranges, unweighted). T = 293.15 to 452.20 K ρ = A + BT + CT 2 + DT 3 + … 1.16268 · 103 −3.59946 · 10−1 −7.45938 · 10−4

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc Ref. (Symbol ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 298.15 990.00 ± 1.00 0.94 0.62 92-sun/dig( ) 44-mor/aue(∆) 381.20 917.70 ± 0.60 293.15 993.00 ± 1.00 −0.06 75-nak/kom( ) 400.60 899.80 ± 0.60 1.02 92-sun/dig( ) 303.30 984.90 ± 0.60 0.01 92-sun/dig( ) 419.50 880.20 ± 0.60 −0.22 92-sun/dig( ) 322.90 968.50 ± 0.60 −0.18 92-sun/dig( ) 439.70 860.00 ± 0.60 −0.20 92-sun/dig( ) 343.60 950.20 ± 0.60 −0.74 92-sun/dig( ) 452.20 847.10 ± 0.60 −0.28 92-sun/dig( ) 361.70 934.00 ± 0.60 −0.90 92-sun/dig( )

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K 290.00 293.15 298.15 300.00 310.00 320.00 330.00

ρ ± σ fit kg ⋅ m−3 995.57 ± 1.20 993.06 ± 1.14 989.06 ± 1.04 987.57 ± 1.01 979.42 ± 0.85 971.12 ± 0.73 962.67 ± 0.64

T K 340.00 350.00 360.00 370.00 380.00 390.00 400.00

ρ ± σ fit kg ⋅ m−3 954.07 ± 0.58 945.33 ± 0.55 936.43 ± 0.54 927.39 ± 0.54 918.19 ± 0.54 908.85 ± 0.56 899.36 ± 0.59

T K 410.00 420.00 430.00 440.00 450.00 460.00

ρ ± σ fit kg ⋅ m−3 889.71 ± 0.62 879.92 ± 0.68 869.98 ± 0.75 859.89 ± 0.84 849.66 ± 0.95 839.27 ± 1.09

cont. Landolt-Börnstein New Series IV/8G

318

3.1.1 Alkanediols, C1 - C6

dl-2,3-Butanediol (cont.)

ρ

ρ

Further references: [1859-wur, 51-wat/coo, 52-cur/joh].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

L-(+)-2,3-Butanediol

[19132-06-0]

C4H10O2

MW = 90.12

657

C4H10O2

MW = 90.12

658

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 46-kno/sch 986.9 ± 0.5

(R*, S*)-2,3-Butanediol

[5341-95-7]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 46-kno/sch 993.9 ± 2.0

Landolt-Börnstein New Series IV/8G

3.1.1 Alkanediols, C1 - C6 2-Methyl-1,2-propanediol

[558-43-0]

C4H10O2

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est ρexp ± 2σ est T T Ref. −3 K K kg ⋅ m kg ⋅ m−3 1) 293.15 37-dob/gut 293.15 1002.4 ± 3.0 996.7 ± 2.0 287.15 37-mou/dod1) 293.15 999.0 ± 3.0 997.0 ± 2.0 293.15 41-hea/tam1) 293.15 1003.0 ± 3.0 996.9 ± 2.0 1) 298.15 48-adk/bil 989.6 ± 3.0 1)

MW = 90.12

659

Ref. 54-vor/tit 65-wei/lan Recommended

Not included in calculation of recommended value.

2-Methyl-1,3-propanediol

[2163-42-0]

C4H10O2

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est ρexp ± 2σ est T T Ref. −3 K K kg ⋅ m kg ⋅ m−3 1) 273.15 07-fav/sok-3 293.15 1029.7 ± 3.0 1009.0 ± 3.0 273.15 07-sok1) 293.15 1029.7 ± 3.0 1020.0 ± 2.0 1) 293.15 35-has/mcb 293.15 1029.0 ± 3.0 1020.0 ± 2.0 293.15 42-pum/hah1) 1027.3 ± 3.0 1)

319

MW = 90.12

660

Ref. 65-bar/koz1) 65-wei/lan Recommended

Not included in calculation of recommended value.

2,2-Dimethyl-1,3-propanediol

[126-30-7]

C5H12O2

MW = 104.15

661

C5H12O2

MW = 104.15

662

C5H12O2

MW = 104.15

663

Table 1. Experimental values with uncertainties. ρexp ± 2σ est T Ref. K kg ⋅ m−3 crystal 298.15 57-ano-10 1066.0 ± 5.0 298.15 60-ano-13 1066.0 ± 5.0 2-Ethyl-1,3-propanediol

[2612-29-5]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K ⋅ kg m 293.15 48-adk/bil 997.0 ± 1.0 2-Methyl-1,3-butanediol

[684-84-4]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est ρexp ± 2σ est T T Ref. −3 K K kg ⋅ m kg ⋅ m−3 1) 293.15 58-far/spe 293.15 994.0 ± 1.5 991.5 ± 1.0 293.15 56-far/she 293.15 991.9 ± 1.0 991.7 ± 1.0 1)

Not included in calculation of recommended value.

Landolt-Börnstein New Series IV/8G

Ref. 64-hel/dav Recommended

320

3.1.1 Alkanediols, C1 - C6

2-Methyl-2,3-butanediol

[5396-58-7]

C5H12O2

MW = 104.15

664

C5H12O2

MW = 104.15

665

C5H12O2

MW = 104.15

666

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 58-hen/wat 968.8 ± 1.0 3-Methyl-1,2-butanediol

[50468-22-9]

Table 1. Experimental values with uncertainties. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 273.15 1875-fla 998.8 ± 2.0 294.65 1875-fla 984.2 ± 2.0 3-Methyl-1,3-butanediol

[2568-33-4]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est ρexp ± 2σ est T T Ref. K K kg ⋅ m−3 kg ⋅ m−3 293.15 07-kut1) 293.15 983.3 ± 3.0 976.3 ± 2.0 273.15 07-kut1) 293.15 995.4 ± 3.0 977.7 ± 2.0 293.15 55-sar/mor1) 293.15 964.5 ± 6.0 977.0 ± 2.1 293.15 57-far/rot1) 986.7 ± 3.0 1)

Ref. 56-far/she 62-esa/shi Recommended

Not included in calculation of recommended value.

1,2-Pentanediol

[5343-92-0]

C5H12O2

MW = 104.15

667

Table 1. Fit with estimated B coefficient for 6 accepted points. Deviation σw = 0.167. Coefficient ρ = A + BT A 1194.93 B −0.760 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. ρexp − ρcalc Ref. ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 273.15 987.0 ± 1.0 1859-wur 293.15 972.3 ± 1.0 0.16 50-cle/mac −0.34 1) 293.15 978.5 ± 3.0 6.36 23-kau/ada 293.15 970.7 ± 2.0 51-cop/fie1) −1.39 297.15 969.1 ± 1.0 0.00 45-len/dup 293.15 972.3 ± 1.0 0.16 62-mel 297.15 969.1 ± 1.0 0.00 45-sch/gel 297.15 969.1 ± 1.0 0.00 62-mel 1)

Not included in calculation of linear coefficients.

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 270.00 989.7 ± 2.3 280.00 982.1 ± 1.4 290.00 974.5 ± 0.7

T K

293.15 298.15

ρexp ± 2σ est kg ⋅ m−3

972.1 ± 0.7 968.3 ± 0.9

Landolt-Börnstein New Series IV/8G

3.1.1 Alkanediols, C1 - C6 1,3-Pentanediol

[3174-67-2]

321

C5H12O2

MW = 104.15

668

C5H12O2

MW = 104.15

669

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 64-hel/dav 981.0 ± 1.0 1,4-Pentanediol

[626-95-9]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est ρexp ± 2σ est T T Ref. −3 K K kg ⋅ m kg ⋅ m−3 1) 273.00 1889-lip 293.15 1000.1 ± 2.0 988.6 ± 1.0 293.15 57-fav/ser 293.15 990.3 ± 1.0 989.5 ± 1.2 1)

Ref. 63-shu/bar Recommended

Not included in calculation of recommended value.

1,5-Pentanediol

[111-29-5]

C5H12O2

MW = 104.15

670

Table 1. Fit with estimated B coefficient for 20 accepted points. Deviation σw = 0.834. Coefficient ρ = A + BT A 1174.56 B −0.620 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T kg ⋅ m−3 kg ⋅ m−3 K K kg ⋅ m−3 kg ⋅ m−3 284.65 987.0 ± 6.0 1893-eyk-11) 318.15 978.5 ± 2.0 1.19 −11.08 351.15 944.5 ± 6.0 1893-eyk-11) 293.15 991.4 ± 1.0 −12.35 −1.41 291.15 994.0 ± 2.0 04-ham 299.15 989.0 ± 1.0 −0.05 −0.09 293.15 992.1 ± 1.0 23-kau/ada 293.15 −0.71 990.4 ± 2.0 −2.41 293.15 993.8 ± 2.0 0.99 27-tri 293.15 990.4 ± 2.0 −2.41 284.15 998.0 ± 1.0 34-pau 293.15 994.3 ± 2.0 1.49 −0.39 299.15 989.0 ± 2.0 45-sch/gel 278.15 1005.9 ± 3.0 3.79 −0.09 293.15 991.4 ± 1.0 50-cle/mac 298.15 997.3 ± 3.0 7.59 −1.41 293.15 992.3 ± 1.0 52-cur/joh 318.15 986.0 ± 3.0 8.69 −0.51 293.15 990.4 ± 2.0 54-ano-12 293.15 992.8 ± 0.4 −2.41 −0.02 293.15 989.0 ± 2.0 55-mos 303.15 986.7 ± 0.4 0.12 −3.81 293.15 994.0 ± 2.0 1.19 57-ket/van 313.15 981.2 ± 0.4 0.84 343.15 962.8 ± 2.0 0.99 57-ket/van 1)

Ref. 57-ket/van 62-mel 62-mel 67-ano-5 68-ano 68-naz/tsy 75-nak/kom1) 75-nak/kom1) 75-nak/kom1) 88-cze/zyw 88-cze/zyw 88-cze/zyw

Not included in calculation of linear coefficients.

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 280.00 1001.0 ± 1.7 290.00 994.8 ± 1.4 293.15 992.8 ± 1.4

Landolt-Börnstein New Series IV/8G

T K 298.15 310.00 320.00

ρexp ± 2σ est −3

kg ⋅ m

989.7 ± 1.3 982.4 ± 1.4 976.2 ± 1.7

T K 330.00 340.00 350.00

ρexp ± 2σ est kg ⋅ m−3

970.0 ± 2.0 963.8 ± 2.4 957.6 ± 2.8

322

3.1.1 Alkanediols, C1 - C6

2,3-Pentanediol

[42027-23-6]

C5H12O2

MW = 104.15

671

C5H12O2

MW = 104.15

672

C6H14O2

MW = 118.18

673

Table 1. Experimental and recommended values with uncertainties. T K 273.15 287.15 273.15 273.15 1)

ρexp ± 2σ est

Ref.

kg ⋅ m−3

994.4 ± 4.0 979.9 ± 4.0 1005.0 ± 1.0 1005.0 ± 1.0

1875-wag/say-11) 1875-wag/say-11) 37-mil/sus Recommended

Not included in calculation of recommended value.

2,4-Pentanediol

[625-69-4]

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 0.900. Coefficient ρ = A + BT A 1201.54 B −0.820 Table 2. Experimental values with uncertainties and deviation from calculated values. T K

293.15 287.15 293.15 298.15 1)

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

963.5 ± 2.0 966.0 ± 1.0 962.3 ± 1.0 956.0 ± 1.0

Ref. 11-zel/arj1) 14-vav 52-cur/joh 72-caz/mar

2.34 −0.08 1.14 −1.06

Not included in calculation of linear coefficients.

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 280.00 971.9 ± 1.7 290.00 963.7 ± 1.2 293.15 961.2 ± 1.1 298.15 957.1 ± 1.2

2,2-Dimethyl-1,3-butanediol

[76-35-7]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 61-ano-11 768.4 ± 1.0

Landolt-Börnstein New Series IV/8G

3.1.1 Alkanediols, C1 - C6 2,2-Dimethyl-1,4-butanediol

[32812-23-0]

323

C6H14O2

MW = 118.18

674

C6H14O2

MW = 118.18

675

C6H14O2

MW = 118.18

676

C6H14O2

MW = 118.18

677

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 277.15 04-bou/bla 996.0 ± 2.0 2,3-Dimethyl-1,3-butanediol

[24893-35-4]

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 0.082. Coefficient ρ = A + BT A 1179.17 B −0.720 Table 2. Experimental values with uncertainties and deviation from calculated values. T K 293.15 298.15 303.15 293.15 1)

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

968.0 ± 0.6 964.5 ± 0.6 961.0 ± 0.6 998.0 ± 10.0

Ref.

−0.10 −0.00 0.10 29.90

53-hat/jou 53-hat/jou 53-hat/jou 57-sar/vor1)

Not included in calculation of linear coefficients.

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 290.00 970.4 ± 0.6 293.15 968.1 ± 0.5 298.15 964.5 ± 0.4 310.00 956.0 ± 0.7 2,3-Dimethyl-1,4-butanediol

[57716-80-0]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 62-raz/bog 977.1 ± 2.0 dl-2,3-Dimethyl-1,4-butanediol

[66553-14-8]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 54-mcc/pro 974.0 ± 2.0

Landolt-Börnstein New Series IV/8G

324 meso-2,3-Dimethyl-1,4-butanediol

3.1.1 Alkanediols, C1 - C6 [500009-29-0]

C6H14O2

MW = 118.18

678

C6H14O2

MW = 118.18

679

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 54-mcc/pro 970.0 ± 2.0

2,3-Dimethyl-2,3-butanediol

[76-09-5]

Table 1. Fit with estimated B coefficient for 5 accepted points. Deviation σw = 0.524. Coefficient ρ = A + BT A 1196.92 B −0.800 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. ρexp − ρcalc Ref. ρexp ± 2σ est ρexp ± 2σ est T T kg ⋅ m−3 kg ⋅ m−3 K K kg ⋅ m−3 kg ⋅ m−3 288.15 966.3 ± 2.0 1884-per 290.15 964.1 ± 2.0 46-lau/wie −0.11 −0.70 298.15 958.0 ± 2.0 1884-per 288.15 967.0 ± 2.0 0.60 52-cur/joh −0.39 288.15 967.0 ± 2.0 0.60 25-vor/wal 293.15 933.0 ± 3.0 52-pet/she1) −29.40 1)

Not included in calculation of linear coefficients.

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 280.00 972.9 ± 1.7 290.00 964.9 ± 1.6 293.15 962.4 ± 1.6 298.15 958.4 ± 1.6

3,3-Dimethyl-1,2-butanediol

[59562-82-2]

C6H14O2

MW = 118.18

680

C6H14O2

MW = 118.18

681

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 323.15 09-cla 940.0 ± 2.0

2-Ethyl-1,3-butanediol

[66553-17-1]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 48-adk/bil 967.7 ± 0.8

Landolt-Börnstein New Series IV/8G

3.1.1 Alkanediols, C1 - C6 2-Ethyl-1,4-butanediol

[57716-79-7]

325

C6H14O2

MW = 118.18

682

C6H14O2

MW = 118.18

683

C6H14O2

MW = 118.18

684

C6H14O2

MW = 118.18

685

C6H14O2

MW = 118.18

686

C6H14O2

MW = 118.18

687

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 14-lon 982.5 ± 2.0 2-Ethyl-2-methyl-1,3-propanediol

[77-84-9]

Table 1. Experimental and recommended values with uncertainties. T K 323.15 323.15 323.15 323.15

ρexp ± 2σ est

Ref.

kg ⋅ m

−3

958.0 ± 1.0 958.0 ± 1.0 958.0 ± 1.0 958.2 ± 1.0

1,2-Hexanediol

58-ano-13 67-ano-5 68-ano Recommended [6920-22-5]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 51-cop/fie 950.7 ± 2.0 1,3-Hexanediol

[21531-91-9]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 295.15 44-gla 958.0 ± 2.0 1,4-Hexanediol

[16432-53-4]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 289.45 44-gla 982.0 ± 2.0 1,5-Hexanediol

[928-40-5]

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 1.120. Coefficient ρ = A + BT A 1215.01 B −0.840 cont.

Landolt-Börnstein New Series IV/8G

326

3.1.1 Alkanediols, C1 - C6

1,5-Hexanediol (cont.) Table 2. Experimental values with uncertainties and deviation from calculated values. T K 293.15 298.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m

kg ⋅ m−3

−3

971.0 ± 2.0 964.0 ± 1.0

Ref.

2.24 -0.56

56-cri 64-ber/lon

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 290.00 971.4 ± 1.9 293.15 968.8 ± 1.8 298.15 964.6 ± 1.8 1,6-Hexanediol

[629-11-8]

C6H14O2

MW = 118.18

688

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 1.678. Coefficient ρ = A + BT A 1183.31 B −0.680 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc ρexp ± 2σ est T Ref. −3 −3 kg ⋅ m K kg ⋅ m 318.55 52-cur/joh1) 957.1 ± 4.0 −9.59 293.15 5.73 63-tsy/sol1) 989.7 ± 2.0 278.15 75-nak/kom 991.8 ± 1.0 −2.37 298.15 1.03 75-nak/kom 981.6 ± 1.0 318.15 1.33 75-nak/kom 968.3 ± 1.0 1)

Not included in calculation of linear coefficients.

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 270.00 999.7 ± 2.3 280.00 992.9 ± 2.0 290.00 986.1 ± 1.8 2,3-Hexanediol

ρexp ± 2σ est

T K 293.15 298.15 310.00

kg ⋅ m−3

984.0 ± 1.8 980.6 ± 1.8 972.5 ± 1.9 [617-30-1]

T K 320.00

C6H14O2

ρexp ± 2σ est kg ⋅ m−3

965.7 ± 2.1

MW = 118.18

689

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 288.15 37-tya 989.0 ± 2.0

Landolt-Börnstein New Series IV/8G

3.1.1 Alkanediols, C1 - C6 2,4-Hexanediol

[19780-90-6]

327

C6H14O2

MW = 118.18

690

C6H14O2

MW = 118.18

691

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 294.15 32-les/wak 951.6 ± 1.0

2,5-Hexanediol

[2935-44-6]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 1.4746 (combined temperature ranges, weighted), σc,uw = 5.9932 · 10−1 (combined temperature ranges, unweighted). T = 273.00 to 343.15 K ρ = A + BT + CT 2 + DT 3 + … 1.00102 · 103 3.21158 · 10−1 −1.57871 · 10−3

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 273.00 966.89 ± 4.00 −4.14 1859-wur(✕ ) 293.15 959.95 ± 0.40 0.46 273.00 966.90 ± 4.00 −4.13 1864-wur(✕ ) 303.15 953.30 ± 0.40 0.01 293.15 961.00 ± 1.00 1.51 02-dud/lem( ) 313.15 946.60 ± 0.40 −0.17 293.15 960.10 ± 1.00 0.61 52-cur/joh( ) 323.15 939.80 ± 0.40 −0.14 293.15 960.00 ± 1.00 0.51 333.15 932.80 ± 0.40 0.01 53-ano-5(∆) 293.15 961.70 ± 2.00 2.21 0.28 62-raz/bog(∇) 343.15 925.60 ± 0.40 293.15 962.50 ± 2.00 3.01 63-shu/bar(◆)

Ref. (Symbol in Fig. 1) 96-gri/zhu(✕ ) 96-gri/zhu(✕ ) 96-gri/zhu(✕ ) 96-gri/zhu(✕ ) 96-gri/zhu(✕ ) 96-gri/zhu(✕ )

Further references: [56-lev/sch, 62-mel].

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

270.00 280.00 290.00 293.15

ρ ± σ fit kg ⋅ m−3 972.64 ± 4.54 967.17 ± 2.76 961.38 ± 1.53 959.49 ± 1.25

T K

298.15 300.00 310.00 320.00

ρ ± σ fit kg ⋅ m−3 956.43 ± 0.89 955.28 ± 0.78 948.86 ± 0.43 942.13 ± 0.34

T K

330.00 340.00 350.00

ρ ± σ fit kg ⋅ m−3 935.08 ± 0.38 927.71 ± 0.58 920.03 ± 0.89

cont.

Landolt-Börnstein New Series IV/8G

328

3.1.1 Alkanediols, C1 - C6

ρ

ρ

2,5-Hexanediol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

3,4-Hexanediol

[922-17-8]

C6H14O2

MW = 118.18

692

C6H14O2

MW = 118.18

693

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 273.15 1859-wur 799.3 ± 20.0

2-Methyl-1,3-pentanediol

[149-31-5]

Table 1. Experimental and recommended values with uncertainties. T K 295.15 293.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

kg ⋅ m

−3

973.7 ± 2.0 971.8 ± 1.0 972.9 ± 1.0 972.3 ± 1.1

43-kul/nor1) 52-cur/joh 60-ano-13 Recommended

Not included in calculation of recommended value.

Landolt-Börnstein New Series IV/8G

3.1.1 Alkanediols, C1 - C6 2-Methyl-1,5-pentanediol

[42856-62-2]

329

C6H14O2

MW = 118.18

694

C6H14O2

MW = 118.18

695

C6H14O2

MW = 118.18

696

Table 1. Experimental and recommended values with uncertainties. T K 293.15 293.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

kg ⋅ m−3

971.9 ± 1.0 971.9 ± 1.0 975.0 ± 2.0 971.9 ± 1.0

51-mca/cul 51-whi/dea 62-yur/rev1) Recommended

Not included in calculation of recommended value.

2-Methyl-2,3-pentanediol

[7795-80-4]

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.200. Coefficient ρ = A + BT A 1167.70 B −0.700 Table 2. Experimental values with uncertainties and deviation from calculated values. T K 293.15 273.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m

kg ⋅ m−3

−3

962.7 ± 1.0 976.3 ± 1.0

0.20 −0.20

Ref. 28-ven-1 28-ven-1

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 270.00 978.7 ± 1.1 280.00 971.7 ± 0.9 290.00 964.7 ± 1.0 293.15 962.5 ± 1.0 298.15 959.0 ± 1.2 2-Methyl-2,4-pentanediol

[107-41-5]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 4.4579 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.7903 · 10−1 (combined temperature ranges, unweighted). Coefficient A B C

T = 273.15 to 343.15 K ρ = A + BT + CT 2 + DT 3 + … 1.09017 · 103 −4.33615 · 10−1 −4.76496 · 10−4 cont.

Landolt-Börnstein New Series IV/8G

330

3.1.1 Alkanediols, C1 - C6

2-Methyl-2,4-pentanediol (cont.) Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc Ref. (Symbol ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) in Fig. 1) ⋅ kg m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 290.15 925.40 ± 2.00 1.16 01-zel/zel(✕ ) 298.15 920.00 ± 1.50 1.47 62-ste/van(◆) 290.15 924.00 ± 1.00 −0.24 303.15 916.00 ± 1.50 1.07 62-ste/van(◆) 12-ost(∆) 290.15 925.40 ± 2.00 1.16 39-dup/dar(✕ ) 293.15 921.60 ± 0.60 −0.51 68-ano( ) 293.15 921.80 ± 1.00 −0.31 293.15 96-gri/zhu(✕ ) 53-ano-5(∇) 921.80 ± 0.40 −0.31 1) 293.15 924.00 ± 2.00 1.89 57-chi/tho 303.15 914.50 ± 0.40 −0.43 96-gri/zhu(✕ ) 298.15 918.10 ± 1.00 −0.43 57-chi/tho(✕ ) 313.15 907.20 ± 0.40 −0.46 96-gri/zhu(✕ ) 273.15 935.50 ± 0.50 −0.68 62-mel( ) 323.15 899.90 ± 0.40 −0.39 96-gri/zhu(✕ ) 293.15 921.60 ± 0.50 −0.51 62-mel( ) 333.15 892.60 ± 0.40 −0.22 96-gri/zhu(✕ ) 303.15 914.50 ± 0.50 −0.43 62-mel( ) 343.15 885.30 ± 0.40 0.03 96-gri/zhu(✕ )

1)

Not included in Fig. 1.

ρ

ρ

Further references: [52-cur/joh, 56-far/she].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

cont.

Landolt-Börnstein New Series IV/8G

3.1.1 Alkanediols, C1 - C6

331

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ).

ρ ± σ fit kg ⋅ m−3

T K

T K

938.36 ± 1.43 931.40 ± 1.25 924.35 ± 1.11 922.11 ± 1.07

270.00 280.00 290.00 293.15

298.15 300.00 310.00 320.00

3-Methyl-1,3-pentanediol

ρ ± σ fit kg ⋅ m−3 918.53 ± 1.02 917.20 ± 1.00 909.96 ± 0.88 902.62 ± 0.77 [33879-72-0]

T K

330.00 340.00 350.00

ρ ± σ fit kg ⋅ m−3 895.19 ± 0.66 887.66 ± 0.59 880.03 ± 0.62

C6H14O2

MW = 118.18

697

C6H14O2

MW = 118.18

698

C6H14O2

MW = 118.18

699

Table 1. Experimental and recommended values with uncertainties. T K 293.15 273.15 290.75 293.15 293.15 1)

ρexp ± 2σ est

Ref.

kg ⋅ m

−3

972.6 ± 3.0 975.5 ± 2.0 965.5 ± 2.0 969.0 ± 1.0 969.0 ± 1.0

32-pfa/pla1) 48-zal1) 48-zal1) 62-esa/shi Recommended

Not included in calculation of recommended value.

3-Methyl-1,5-pentanediol

[4457-71-0]

Table 1. Experimental and recommended values with uncertainties. T K 293.15 293.15 293.15 293.15 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

973.8 ± 1.0 973.8 ± 1.0 972.6 ± 1.0 973.8 ± 1.0 973.5 ± 1.0

51-mca/cul 51-whi/dea 55-blo/ver-1 56-ano-3 Recommended

3-Methyl-2,3-pentanediol

[63521-37-9]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est

T K

293.15 288.15 298.15 298.15 1)

Ref.

kg ⋅ m

−3

970.1 ± 2.0 975.0 ± 2.0 963.8 ± 1.0 963.8 ± 1.0

52-van1) 52-van1) 58-hen/wat Recommended

Not included in calculation of recommended value.

Landolt-Börnstein New Series IV/8G

332

3.1.1 Alkanediols, C1 - C6

3-Methyl-2,4-pentanediol

[5683-44-3]

C6H14O2

MW = 118.18

700

C6H14O2

MW = 118.18

701

C6H14O2

MW = 118.18

702

C6H14O2

MW = 118.18

703

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 287.15 01-zel/zel 990.6 ± 2.0

4-Methyl-1,4-pentanediol

[1462-10-8]

Table 1. Experimental and recommended values with uncertainties. T K

290.15 293.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

965.1 ± 2.0 964.5 ± 1.0 970.0 ± 2.0 964.5 ± 1.0

52-wil/sch1) 55-sar/mor 58-col/fal1) Recommended

Not included in calculation of recommended value.

2-(1-Methylethyl)-1,3-propanediol

[2612-27-3]

Table 1. Experimental values with uncertainties. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 53-pin/hun 976.2 ± 1.0 293.15 62-bog/osi 977.0 ± 0.5 293.15 Recommended 976.8 ± 0.5

2-Propyl-1,3-propanediol

[2612-28-4]

Table 1. Experimental and recommended values with uncertainties. T K

298.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

963.6 ± 2.0 965.9 ± 0.5 965.9 ± 0.5

48-adk/bil1) 62-bog/osi Recommended

Not included in calculation of recommended value.

Landolt-Börnstein New Series IV/8G

3.1.2 Alkanediols, C7 - C14

333

3.1.2 Alkanediols, C7 - C14 2-Butyl-1,3-propanediol

[2612-26-2]

C7H16O2

MW = 132.2

704

C7H16O2

MW = 132.2

705

C7H16O2

MW = 132.2

706

C7H16O2

MW = 132.2

707

C7H16O2

MW = 132.2

708

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

946.1 ± 1.0

48-adk/bil

2,2-Diethyl-1,3-propanediol

[115-76-4]

Table 1. Experimental values with uncertainties. ρexp ± 2σ est

T K

293.15 293.15 293.15 334.45 334.45

Ref.

−3

kg ⋅ m

crystal 1052.0 ± 5.0 1052.0 ± 5.0 1052.0 ± 5.0 liquid 949.0 ± 2.0 949.0 ± 2.0

54-ano-12 60-ano-13 62-mel 54-ano-12 60-ano-13

2,3-Dimethyl-1,3-pentanediol

[66225-52-3]

Table 1. Experimental value with uncertainty. T K 296.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

957.0 ± 1.0

53-col/dre

2,3-Dimethyl-2,3-pentanediol

[6931-70-0]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

−3

kg ⋅ m

961.3 ± 2.0

41-fav/oni

(R*,S*)-2,4-Dimethyl-1,5-Pentanediol

[3817-48-9]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

kg ⋅ m−3

945.0 ± 2.0

Landolt-Börnstein New Series IV/8G

55-nol/pan

334

3.1.2 Alkanediols, C7 - C14

2,4-Dimethyl-2,4-pentanediol

[24892-49-7]

C7H16O2

MW = 132.2

709

C7H16O2

MW = 132.2

710

C7H16O2

MW = 132.2

711

C7H16O2

MW = 132.2

712

C7H16O2

MW = 132.2

713

C7H16O2

MW = 132.2

714

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

920.6 ± 2.0

09-lem-1

3,4-Dimethyl-1,4-pentanediol

[63521-36-8]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

952.8 ± 1.0

57-sar/vor

2-Ethyl-1,5-pentanediol

[14189-13-0]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

967.9 ± 1.0

62-yur/rev

2-Ethyl-2,4-pentanediol

[38836-25-8]

Table 1. Experimental and recommended values with uncertainties. T K 293.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

kg ⋅ m−3

920.6 ± 4.0 929.6 ± 2.0 929.6 ± 2.0

09-lem1) 63-esa Recommended

Not included in calculation of recommended value.

3-Ethylpentane-2,3-diol

[66225-32-9]

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

961.2 ± 2.0

1,4-Heptanediol

58-hen/wat [40646-07-9]

Table 1. Fit with estimated B coefficient for 4 accepted points. Deviation σw = 0.173. Coefficient ρ = A + BT 1158.80 A B −0.700 cont. Landolt-Börnstein New Series IV/8G

3.1.2 Alkanediols, C7 - C14

335

Table 2. Experimental values with uncertainties and deviation from calculated values. T K 293.15 298.15 288.15 288.15 288.15 1)

ρexp ± 2σ est

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−3

kg ⋅ m

954.3 ± 2.0 950.4 ± 1.0 957.0 ± 1.0 957.0 ± 1.0 957.0 ± 1.0

27-bra/ada1) 34-bur/adk 51-gor 51-gor 52-roe/stu

0.70 0.30 −0.10 −0.10 −0.10

Not included in calculation of linear coefficients.

Table 3. Recommended values. ρexp ± 2σ est

T K 280.00 290.00

ρexp ± 2σ est

T K 293.15 298.15

−3

kg ⋅ m

962.8 ± 1.3 955.8 ± 0.7

1,5-Heptanediol

kg ⋅ m−3

953.6 ± 0.8 950.1 ± 1.1 [60096-09-5]

C7H16O2

MW = 132.2

715

C7H16O2

MW = 132.2

716

C7H16O2

MW = 132.2

717

Table 1. Experimental and recommended values with uncertainties. T K 293.15 288.15 293.15 1)

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

970.5 ± 2.0 962.0 ± 6.0 970.5 ± 2.0

25-pie/ada 35-pau-21) Recommended

Not included in calculation of recommended value.

1,6-Heptanediol

[13175-27-4]

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

962.0 ± 2.0

1,7-Heptanediol

66-bue [629-30-1]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 1.9518 · 10−2 (combined temperature ranges, weighted), σc,uw = 9.7590 · 10−3 (combined temperature ranges, unweighted). Coefficient A B C

T = 293.15 to 343.15 K ρ = A + BT + CT 2 + DT 3 + … 1.12164 · 103 −5.46836 · 10−1 −7.14286 · 10−5 cont.

Landolt-Börnstein New Series IV/8G

336

3.1.2 Alkanediols, C7 - C14

1,7-Heptanediol (cont.) Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

−3

kg ⋅ m

293.15 955.20 ± 0.50 303.15 949.30 ± 0.50 313.15 943.40 ± 0.50

ρexp − ρcalc kg ⋅ m

Ref. (Symbol in Fig. 1)

0.00 −0.01 0.00

96-gri/zhu( ) 96-gri/zhu( ) 96-gri/zhu( )

−3

T K

ρexp ± 2σ est

ρexp − ρcalc kg ⋅ m

Ref. (Symbol in Fig. 1)

0.03 −0.04 0.01

96-gri/zhu( ) 96-gri/zhu( ) 96-gri/zhu( )

−3

−3

kg ⋅ m

323.15 937.50 ± 0.50 333.15 931.50 ± 0.50 343.15 925.60 ± 0.50

ρ

ρ

Further references: [34-bur/adk, 51-hub, 64-pol/bel].

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

290.00 293.15 298.15

ρ ± σ fit kg ⋅ m−3 957.05 ± 0.83 955.20 ± 0.74 952.25 ± 0.62

T K

300.00 310.00 320.00

ρ ± σ fit kg ⋅ m−3 951.16 ± 0.59 945.26 ± 0.51 939.34 ± 0.48

T K

330.00 340.00 350.00

ρ ± σ fit kg ⋅ m−3 933.41 ± 0.49 927.46 ± 0.67 921.50 ± 1.13

Landolt-Börnstein New Series IV/8G

3.1.2 Alkanediols, C7 - C14 2,4-Heptanediol

[20748-86-1]

C7H16O2

337 MW = 132.2

718

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.100.

ρ = A + BT

Coefficient A B

1134.61 −0.700

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc ρexp ± 2σ est T Ref. kg ⋅ m−3 K kg ⋅ m−3

298.15 288.15

926.0 ± 1.0 932.8 ± 1.0

0.10 −0.10

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 938.6 ± 1.1 931.6 ± 0.9

280.00 290.00

39-stu/adk 47-dev ρexp ± 2σ est

T K 293.15 298.15

3,4-Heptanediol

kg ⋅ m−3

929.4 ± 0.9 925.9 ± 0.9

[62593-33-3]

C7H16O2

MW = 132.2

719

[66225-35-2]

C7H16O2

MW = 132.2

720

[1462-11-9]

C7H16O2

MW = 132.2

721

[66225-37-4]

C7H16O2

MW = 132.2

722

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 295.15 295.15 1)

945.7 ± 2.0 943.0 ± 1.0 943.0 ± 1.0

25-pie/ada1) 36-wie Recommended

Not included in calculation of recommended value.

2-Methyl-2,4-hexanediol Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 291.15

932.1 ± 1.0

26-pas/zam

2-Methyl-2,6-hexanediol Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 295.15 56-cri 967.0 ± 2.0

4-Methyl-1,5-hexanediol

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 62-yur/pen 966.3 ± 2.0 Landolt-Börnstein New Series IV/8G

338

3.1.2 Alkanediols, C7 - C14

2-Methyl-2-propyl-1,3-propanediol

[78-26-2]

C7H16O2

MW = 132.2

723

C7H16O2

MW = 132.2

724

C7H16O2

MW = 132.2

725

C8H18O2

MW = 146.23

726

C8H18O2

MW = 146.23

727

C8H18O2

MW = 146.23

728

Table 1. Experimental and recommended values with uncertainties. T K

293.15 293.15 293.15 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

857.0 ± 1.0 857.1 ± 1.0 858.5 ± 1.0 857.5 ± 1.1

54-ano-12 59-ano-7 60-ano-13 Recommended

2-(1-Methylethyl)-1,4-butanediol

[39497-66-0]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

967.2 ± 0.8

54-fre/lwo

2-Propyl-1,4-butanediol

[62946-68-3]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

962.5 ± 2.0

14-lon

2,4-Dimethyl-2,4-hexanediol

[29649-22-7]

Table 1. Experimental value with uncertainty. T K

293.35

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

922.9 ± 2.0

34-jac-5

2,5-Dimethyl-2,4-hexanediol

[3899-89-6]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

917.2 ± 2.0

64-esa/das

3,4-Dimethyl-2,4-hexanediol

[900002-90-6]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

938.2 ± 2.0

62-fav/por

Landolt-Börnstein New Series IV/8G

3.1.2 Alkanediols, C7 - C14 3,5-Dimethyl-2,3-hexanediol

[99799-29-8]

339

C8H18O2

MW = 146.23

729

C8H18O2

MW = 146.23

730

C8H18O2

MW = 146.23

731

C8H18O2

MW = 146.23

732

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est

T K

293.15 298.15 298.15 1)

Ref.

−3

kg ⋅ m

915.7 ± 2.0 928.5 ± 1.0 928.5 ± 1.0

51-ber-21) 58-hen/wat Recommended

Not included in calculation of recommended value.

2-Ethyl-1,3-hexanediol

[94-96-2]

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 0.176. Coefficient ρ = A + BT 1180.92 A B −0.820 Table 2. Experimental values with uncertainties and deviation from calculated values. T K 295.15 293.15 293.15

ρexp ± 2σ est

ρexp − ρcalc

kg ⋅ m−3

kg ⋅ m−3

938.4 ± 2.0 940.6 ± 1.0 940.6 ± 1.0

Ref.

−0.50 0.06 0.06

64-bla/per-1 53-ano-15 62-mel

Table 3. Recommended values. ρexp ± 2σ est

T K 290.00 293.15 298.15

kg ⋅ m−3

943.1 ± 1.3 940.5 ± 1.2 936.4 ± 1.3

2-Ethyl-1-methyl-1,5-pentanediol

[900002-72-4]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

kg ⋅ m−3

960.0 ± 2.0

62-yur/rev

4-Ethyl-1,4-hexanediol

[1113-00-4]

Table 1. Experimental value with uncertainty. T K 292.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

970.4 ± 1.0

Landolt-Börnstein New Series IV/8G

51-gor

340

3.1.2 Alkanediols, C7 - C14

4-Ethyl-1,5-hexanediol

[90951-82-9]

C8H18O2

MW = 146.23

733

C8H18O2

MW = 146.23

734

C8H18O2

MW = 146.23

735

C8H18O2

MW = 146.23

736

C8H18O2

MW = 146.23

737

C8H18O2

MW = 146.23

738

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

960.0 ± 2.0

62-yur/pen

2-Methyl-2,3-heptanediol

[1068-81-1]

Table 1. Experimental value with uncertainty. T K

298.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

929.0 ± 2.0

64-col/var

3-Methyl-3,5-heptanediol

[99799-27-6]

Table 1. Experimental values with uncertainties. T K

291.15 294.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

929.9 ± 2.0 928.0 ± 2.0

26-pas/zam 51-dub

5-Methyl-1,5-heptanediol

[99799-26-5]

Table 1. Experimental value with uncertainty. T K

292.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

961.0 ± 2.0

56-cri

5-Methyl-2,4-heptanediol

[500014-48-2]

Table 1. Experimental value with uncertainty. T K

298.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

928.0 ± 2.0

39-stu/adk

6-Methyl-1,6-heptanediol

[5392-57-4]

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

959.0 ± 2.0

66-bue

Landolt-Börnstein New Series IV/8G

3.1.2 Alkanediols, C7 - C14 2-(1-Methylethyl)-1,5-pentanediol

[90951-89-6]

341

C8H18O2

MW = 146.23

739

C8H18O2

MW = 146.23

740

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

956.1 ± 2.0

62-yur/rev

1,5-Octanediol

[2736-67-6]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est

T K

290.15 289.15 1)

T K

Ref.

−3

kg ⋅ m

949.0 ± 2.0 946.0 ± 2.0

35-pau-21) 56-cri1)

298.15 298.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

949.0 ± 1.0 949.0 ± 1.0

66-bue-1 Recommended

Not included in calculation of recommended value.

1,6-Octanediol

[4066-76-6]

C8H18O2

MW = 146.23

741

C8H18O2

MW = 146.23

742

C8H18O2

MW = 146.23

743

C8H18O2

MW = 146.23

744

Table 1. Experimental values with uncertainties. ρexp ± 2σ est

T K

288.15 298.15

Ref.

−3

kg ⋅ m

943.0 ± 3.0 954.0 ± 3.0

65-mor/lam 66-bue

1,7-Octanediol

[13175-32-1]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est

T K

298.15 298.15 298.15

Ref.

kg ⋅ m−3

942.0 ± 1.0 944.0 ± 1.0 943.0 ± 1.2

62-col/gir 66-bue Recommended

2,4-Octanediol

[90162-24-6]

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

918.0 ± 2.0

39-stu/adk

2-Propyl-1,5-pentanediol

[90951-90-9]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

953.0 ± 2.0

Landolt-Börnstein New Series IV/8G

62-yur/rev

342

3.1.2 Alkanediols, C7 - C14

2,2,4-Trimethyl-1,3-pentanediol

[144-19-4]

C8H18O2

MW = 146.23

745

MW = 160.26

746

Table 1. Experimental and recommended values with uncertainties. T K 296.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

961.0 ± 10.0 922.9 ± 1.0 922.9 ± 1.0

43-kul/nor1) 59-ano-7 Recommended

Not included in calculation of recommended value.

2-Butyl-2-ethyl-1,3-propanediol

[115-84-4]

C9H20O2

Table 1. Experimental and recommended values with uncertainties. T K 323.15 323.15 1)

ρexp ± 2σ est

T K 323.15 323.15

Ref.

−3

kg ⋅ m

929.0 ± 1.0 929.0 ± 1.0

53-ano-15 60-ano-13

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

931.0 ± 2.0 929.0 ± 1.0

62-mel1) Recommended

Not included in calculation of recommended value.

2-Butyl-1,5-pentanediol

[90724-91-7]

C9H20O2

MW = 160.26

747

C9H20O2

MW = 160.26

748

C9H20O2

MW = 160.26

749

C9H20O2

MW = 160.26

750

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

941.4 ± 2.0

62-yur/rev

2,4-Dimethyl-2,4-heptanediol

[59194-83-1]

Table 1. Experimental value with uncertainty. T K

290.35

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

913.8 ± 2.0

34-jac-5

2,4-Dimethyl-2,6-heptanediol

[73264-94-5]

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

920.0 ± 1.5

64-hin/dre

2,5-Dimethyl-3,5-heptanediol

[3955-69-9]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

915.6 ± 2.0

64-esa/das

Landolt-Börnstein New Series IV/8G

3.1.2 Alkanediols, C7 - C14 2,6-Dimethyl-2,4-heptanediol

[73264-93-4]

343

C9H20O2

MW = 160.26

751

C9H20O2

MW = 160.26

752

C9H20O2

MW = 160.26

753

C9H20O2

MW = 160.26

754

C9H20O2

MW = 160.26

755

C9H20O2

MW = 160.26

756

C9H20O2

MW = 160.26

757

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 291.15 26-pas/zam 902.0 ± 2.0 4,4-Dimethyl-1,7-heptanediol

[900002-74-6]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 55-blo/whe 939.0 ± 1.0 4-Ethyl-1,4-heptanediol

[900002-73-5]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 64-des/sou 970.0 ± 2.0 5-Ethyl-1,5-heptanediol

[57740-06-4]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 291.15 56-cri 958.0 ± 2.0 3-Methyl-3,5-octanediol

[38836-28-1]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 62-esa/zhu 916.0 ± 1.0 4-Methyl-2,4-octanediol

[38836-27-0]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 63-esa 911.7 ± 1.0 6-Methyl-1,6-octanediol

[13175-25-2]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 298.15 66-bue 952.0 ± 2.0 Landolt-Börnstein New Series IV/8G

344

3.1.2 Alkanediols, C7 - C14

6-Methyl-1,7-octanediol

[91391-44-5]

C9H20O2

MW = 160.26

758

C9H20O2

MW = 160.26

759

C9H20O2

MW = 160.26

760

C9H20O2

MW = 160.26

761

C9H20O2

MW = 160.26

762

C9H20O2

MW = 160.26

763

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

953.0 ± 2.0

62-col/gir

7-Methyl-1,7-octanediol

[13175-30-9]

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

938.0 ± 2.0

66-bue

1-Methyl-2-propyl-1,5-pentanediol

[900002-75-7]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

954.3 ± 2.0

62-yur/pen

2-(2-Methylpropyl)-1,5-pentanediol

[57740-10-0]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

941.6 ± 2.0

62-yur/rev

1,4-Nonanediol

[2430-73-1]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

929.5 ± 1.0

62-nik/vor

1,5-Nonanediol

[13686-96-9]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

937.0 ± 1.0

25-pie/ada

Landolt-Börnstein New Series IV/8G

3.1.2 Alkanediols, C7 - C14 1,6-Nonanediol

[4066-78-8]

345

C9H20O2

MW = 160.26

764

C9H20O2

MW = 160.26

765

C9H20O2

MW = 160.26

766

C9H20O2

MW = 160.26

767

C 10H22O2

MW = 174.28

768

C10H22O2

MW = 174.28

769

Table 1. Experimental values with uncertainties. T K 294.15 298.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

935.0 ± 3.0 941.0 ± 3.0

65-mor/lam 66-bue

1,7-Nonanediol

[4469-84-5]

Table 1. Experimental value with uncertainty. T K 298.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

944.0 ± 2.0

66-bue

4-Propyl-1,5-hexanediol

[13687-05-3]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

kg ⋅ m−3

954.3 ± 2.0

62-yur/pen

2,4,5-Trimethyl-2,4-hexanediol

[36587-81-2]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

301.35

Ref.

kg ⋅ m−3

920.7 ± 2.0

34-jac-5

1,4-Decanediol

[37810-94-9]

Table 1. Experimental values with uncertainties. ρexp ± 2σ est

T K

293.15 293.15 293.15

Ref.

−3

kg ⋅ m

922.0 ± 2.0 917.6 ± 1.0 917.6 ± 1.0

62-nik/vor 51-gor 52-roe/stu

1,7-Decanediol

[13175-33-2]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

298.15

Ref.

−3

kg ⋅ m

929.0 ± 2.0

Landolt-Börnstein New Series IV/8G

66-bue

346

3.1.2 Alkanediols, C7 - C14

1,10-Decanediol

[112-47-0]

C10H22O2

MW = 174.28

770

Table 1. Fit with estimated B coefficient for 4 accepted points. Deviation σw = 2.320. Coefficient ρ = A + BT 1151.52 A B −0.755 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc ρexp ± 2σ est T Ref. kg ⋅ m−3 K kg ⋅ m−3 crystal 298.15 62-par/mos 1100.0 ± 5.0 liquid 353.15 50-boe/ned 883.0 ± 1.5 −1.89 403.15 2.86 50-boe/ned 850.0 ± 2.0 453.15 2.61 50-boe/ned 812.0 ± 2.0 513.15 50-boe/ned 762.0 ± 2.0 −2.09 Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 350.00 887.3 ± 4.4 360.00 879.7 ± 4.1 370.00 872.2 ± 3.7 380.00 864.6 ± 3.4 390.00 857.1 ± 3.2 400.00 849.5 ± 3.0 2,5-Diethyl-1,6-hexanediol

ρexp ± 2σ est

T K 410.00 420.00 430.00 440.00 450.00 460.00

−3

kg ⋅ m

842.0 ± 2.9 834.4 ± 2.9 826.9 ± 2.9 819.3 ± 3.1 811.8 ± 3.3 804.2 ± 3.5 [91241-30-4]

T K 470.00 480.00 490.00 500.00 510.00 520.00

ρexp ± 2σ est kg ⋅ m−3

796.7 ± 3.9 789.1 ± 4.2 781.6 ± 4.6 774.0 ± 5.0 766.5 ± 5.4 758.9 ± 5.8

C10H22O2

MW = 174.28

771

C10H22O2

MW = 174.28

772

C10H22O2

MW = 174.28

773

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 38-hil/adk 930.7 ± 1.0 3,4-Diethyl-3,4-hexanediol

[6931-71-1]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 79-bal/fri 943.5 ± 0.2 2,4-Dimethyl-2,4-octanediol

[7177-01-7]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 294.65 34-jac-5 902.0 ± 1.0 Landolt-Börnstein New Series IV/8G

3.1.2 Alkanediols, C7 - C14 2,5-Dimethyl-3,5-octanediol

[3899-88-5]

347

C10H22O2

MW = 174.28

774

C10H22O2

MW = 174.28

775

C10H22O2

MW = 174.28

776

C10H22O2

MW = 174.28

777

C10H22O2

MW = 174.28

778

C10H22O2

MW = 174.28

779

C10H22O2

MW = 174.28

780

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 64-esa/das 909.7 ± 2.0 3,7-Dimethyl-1,6-octanediol

[53067-10-0]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 32-lon/kha 948.1 ± 2.0 3,7-Dimethyl-1,7-octanediol

[107-74-4]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 42-mul 926.0 ± 2.0 3,7-Dimethyl-3,5-octanediol

[56548-45-9]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 285.15 26-pas/zam 911.8 ± 2.0 3,4-Dimethyl-3,4-octanediol

[91179-88-3]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 64-nog/rtv 932.6 ± 1.0 3,7-Dimethyl-1,3-octanediol

[102880-60-4]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 32-pfa/pla 916.5 ± 2.0 2,3-Dipropyl-1,4-butanediol

[74854-17-4]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 39-mar/wil 936.2 ± 2.0

Landolt-Börnstein New Series IV/8G

348

3.1.2 Alkanediols, C7 - C14

4-Ethyl-3,5-octanediol

[900002-77-9]

C10H22O2

MW = 174.28

781

C10H22O2

MW = 174.28

782

C10H22O2

MW = 174.28

783

C10H22O2

MW = 174.28

784

C10H22O2

MW = 174.28

785

C10H22O2

MW = 174.28

786

C10H22O2

MW = 174.28

787

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 51-dra-1 926.3 ± 1.0 6-Methyl-2-(1-methylethyl)-1,3-hexanediol

[900002-78-0]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 296.15 43-kul/nor 916.1 ± 2.0 2-Methyl-2,3-nonanediol

[900002-76-8]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 273.15 26-nic 937.5 ± 2.0 6-Methyl-1,6-nonanediol

[13175-26-3]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 298.15 66-bue 942.0 ± 2.0 7-Methyl-1,7-nonanediol

[13379-31-2]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 66-bue 934.0 ± 2.0 2-Propyl-1,3-heptanediol

[6628-65-5]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 301.15 43-kul/nor 915.5 ± 2.0 2,4,6-Trimethyl-2,4-heptanediol

[33070-42-7]

Table 1. Fit with estimated B coefficient for 3 accepted points. Deviation σw = 0.696. Coefficient ρ = A + BT 1117.71 A B −0.720 cont. Landolt-Börnstein New Series IV/8G

3.1.2 Alkanediols, C7 - C14

349

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp ± 2σ est

T K

293.15 288.15 292.35

ρexp − ρcalc

Ref.

kg ⋅ m−3

−3

kg ⋅ m

906.1 ± 2.0 909.8 ± 2.0 908.2 ± 2.0

−0.54 −0.44 0.98

31-deg 31-deg 34-jac-5

Table 3. Recommended values. T K

280.00 290.00

ρexp ± 2σ est −3

kg ⋅ m

916.1 ± 2.0 908.9 ± 1.9

4,4-Diethyl-1,7-heptanediol

ρexp ± 2σ est

T K

kg ⋅ m−3

906.6 ± 1.9 903.0 ± 2.0

293.15 298.15

[72936-15-3]

C11H24O2

MW = 188.31

788

C11H24O2

MW = 188.31

789

C11H24O2

MW = 188.31

790

C11H24O2

MW = 188.31

791

C11H24O2

MW = 188.31

792

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 79-zel/hub 953.0 ± 2.0 2,4-Dimethyl-2,4-nonanediol

[69201-96-3]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 299.75 34-jac-5 896.3 ± 2.0 3-Methyl-3,4-decanediol

[900002-79-1]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 273.15 26-nic 940.0 ± 2.0 7-Methyl-1,7-decanediol

[13175-31-0]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 66-bue 929.0 ± 2.0 2,4,7-Trimethyl-2,4-octanediol

[900002-80-4]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 295.35 34-jac-5 896.1 ± 2.0

Landolt-Börnstein New Series IV/8G

350 1,4-Undecanediol

3.1.2 Alkanediols, C7 - C14 [4272-02-0]

C11H24O2

MW = 188.31

793

C11H24O2

MW = 188.31

794

C12H26O2

MW = 202.34

795

C12H26O2

MW = 202.34

796

C13H28O2

MW = 216.36

797

C13H28O2

MW = 216.36

798

C14H30O2

MW = 230.39

799

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 65-das/mae 915.7 ± 1.0 1,5-Undecanediol

[13686-98-1]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 294.15 56-cri 914.0 ± 2.0 2-Butyl-1,3-octanediol

[55109-62-1]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 43-kul/nor 918.4 ± 2.0 4-Methyl-4,5-undecanediol

[900002-81-5]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 273.15 26-nic 935.5 ± 2.0 2-Methyl-1,4-dodecanediol

[92153-96-3]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 62-nik/vor 897.2 ± 2.0 3-Methyl-1,3-dodecanediol

[900002-82-6]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 293.15 32-pfa/pla 902.0 ± 2.0 2-Pentyl-1,3-nonanediol

[55109-63-2]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 296.15 43-kul/nor 898.4 ± 2.0 Landolt-Börnstein New Series IV/8G

3.2.1 Unsaturated Diols of General Formula CnH2nO2

351

3.2 Unsaturated Diols 3.2.1 Unsaturated Diols of General Formula CnH2nO2 2-Butene-1,4-diol

[110-64-5]

C4H8O2

MW = 88.11

800

C4H8O2

MW = 88.11

801

C4H8O2

MW = 88.11

802

C5H10O2

MW = 102.13

803

Table 1. Experimental values with uncertainties. T K 288.15 293.15 293.15 298.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

1082.0 ± 3.0 1080.0 ± 3.0 1080.0 ± 3.0 1080.0 ± 3.0

46-pre/val 48-pud 48-val 78-ovc/kry

(E)-2-Butene-1,4-diol

[821-11-4]

Table 1. Experimental and recommended values with uncertainties. ρexp ± 2σ est

T K

293.15 293.15 293.15

Ref.

−3

kg ⋅ m

1068.7 ± 1.0 1068.5 ± 0.8 1068.6 ± 0.8

52-cur/joh 56-smi/ebe Recommended

(Z)-2-Butene-1,4-diol

[6117-80-2]

Table 1. Experimental and recommended values with uncertainties. T K 293.15 294.15 293.15 293.15 1)

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

1069.8 ± 2.0 1069.9 ± 2.0 1074.0 ± 0.8 1074.0 ± 0.8

28-pre-41) 44-pre1) 56-smi/ebe Recommended

Not included in calculation of recommended value.

(Z)-2-Pentene-1,4-diol

[500036-05-5]

Table 1. Experimental value with uncertainty. T K 291.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

1017.0 ± 2.0

Landolt-Börnstein New Series IV/8G

51-gor

352

3.2.1 Unsaturated Diols of General Formula CnH2nO2

(Z)-4-Methyl-2-pentene-1,4-diol

[500036-09-9]

C6H12O2

MW = 116.16

804

C7H14O2

MW = 130.19

805

C7H14O2

MW = 130.19

806

C8H16O2

MW = 144.21

807

C8H16O2

MW = 144.21

808

C9H18O2

MW = 158.24

809

Table 1. Experimental value with uncertainty. T K 290.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

990.0 ± 2.0

51-gor

(Z)-2-Heptene-1,4-diol

[83726-19-6]

Table 1. Experimental value with uncertainty. T K 299.65

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

970.0 ± 2.0

51-gor

5-Methyl-3-hexene-1,5-diol

[19764-75-1]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

980.2 ± 1.0

67-min/che

(Z)-4-Ethyl-2-hexene-1,4-diol

[500036-10-2]

Table 1. Experimental value with uncertainty. T K 288.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

974.0 ± 0.0

51-gor

5-Methyl-3-heptene-1,5-diol

[19764-76-2]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

972.5 ± 1.0

67-min/che

5-Methyl-3-octene-1,5-diol

[19764-77-3]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

955.5 ± 1.0

67-min/che

Landolt-Börnstein New Series IV/8G

3.2.1 Unsaturated Diols of General Formula CnH2nO2 (Z)-2-Decene-1,4-diol

[500036-07-7]

353

C10H20O2

MW = 172.27

810

C10H20O2

MW = 172.27

811

C12H24O2

MW = 200.32

812

C14H28O2

MW = 228.38

813

Table 1. Experimental value with uncertainty. T K 295.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

930.0 ± 2.0

51-gor

3,4-Dimethyl-5-octene-3,4-diol

[91008-98-9]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

970.4 ± 2.0

64-nog/rtv

2-Dodecene-1,4-diol

[97029-80-6]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

293.15

Ref.

kg ⋅ m−3

934.3 ± 2.0

62-nik/vor

6,7-Diethyl-3-methyl-6-nonene-3,4-diol

[20368-03-0]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

921.2 ± 1.0

Landolt-Börnstein New Series IV/8G

67-zal/aru

3.2.2 Unsaturated Diols of general formula CnH2n-2O2

355

3.2.2 Unsaturated Diols of General Formula CnH2n-2O2 2-Butyne-1,4-diol

[110-65-6]

C4H6O2

MW = 86.09

814

C5H8O2

MW = 100.12

815

C6H10O2

MW = 114.14

816

C6H10O2

MW = 114.14

817

C7H12O2

MW = 128.17

818

C7H12O2

MW = 128.17

819

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

1100.1 ± 0.0

66 -koz/rab

2-Pentyne-1,4-diol

[927-57-1]

Table 1. Experimental value with uncertainty. T K 290.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

1072.0 ± 1.5

51-gor

2-Methyl-3-pentyne-2,5-diol

[900002-87-1]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

1029.1 ± 1.0

66-vla/vas

4-Methyl-2-pentyne-1,4-diol

[10605-66-0]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

290.15

Ref.

−3

kg ⋅ m

1029.0 ± 2.5

51-gor

2-Heptyne-1,4-diol

[18864-39-6]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est

T K

288.15

Ref.

−3

kg ⋅ m

1012.4 ± 1.5

51-gor

4-Methyl-2-hexyne-1,4-diol

[920-09-2]

Table 1. Experimental value with uncertainty. T K 293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

1022.40 ± 1.0

Landolt-Börnstein New Series IV/8G

66-vla/vas

356

3.2.2 Unsaturated Diols of general formula CnH2n-2O2

4-Ethyl-2-hexyne-1,4-diol

[163005-62-7]

C8H14O2

MW = 142.2

820

C8H14O2

MW = 142.2

821

C10H18O2

MW = 170.25

822

C10H18O2

MW = 170.25

823

Table 1. Experimental value with uncertainty. T K 291.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

1000.5 ± 2.0

51-gor

4-Methyl-2-heptyne-1,4-diol

[10605-67-1]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

kg ⋅ m−3

996.5 ± 1.0

66-vla/vas

2-Decyne-1,4-diol

[71393-78-7]

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 0.200. Coefficient ρ = A + BT 1148.34 A B −0.680 Table 2. Experimental values with uncertainties and deviation from calculated values. T K 273.15 293.15

ρexp ± 2σ est −3

kg ⋅ m

962.4 ± 1.0 949.2 ± 1.0

ρexp − ρcalc

Ref.

−3

kg ⋅ m

−0.20 0.20

51-gor 51-gor

Table 3. Recommended values. T K 270.00 280.00 290.00 293.15 298.15

ρexp ± 2σ est kg ⋅ m−3

964.7 ± 1.1 957.9 ± 0.9 951.1 ± 1.0 949.0 ± 1.0 945.6 ± 1.2

3,4-Dimethyl-5-octyne-3,4-diol

[92490-84-1]

Table 1. Experimental value with uncertainty. T K

293.15

ρexp ± 2σ est

Ref.

−3

kg ⋅ m

964.2 ± 2.0

64-nog/rtv

Landolt-Börnstein New Series IV/8G

4 Triols

357

4 Tabulated Data on Density - Triols 1,2,3-Propanetriol

[56-81-5]

C3H8O3

MW = 92.09

824

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 5.4871 · 10−1 (combined temperature ranges, weighted), σc,uw = 1.5204 · 10−1 (combined temperature ranges, unweighted). Coefficient A B C

T = 288.15 to 533.15 K ρ = A + BT + CT 2 + DT 3 + … 1.43632 · 103 −5.28889 · 10−1 −2.29556 · 10−4

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 1) kg ⋅ m kg ⋅ m−3 K K kg ⋅ m kg ⋅ m 293.15 1259.40 ± 1.00 −2.15 1864-lan(✕ ) 333.15 1234.00 ± 1.00 −0.64 291.15 1264.60 ± 1.00 1.72 07-che-1(✕ ) 353.15 1220.00 ± 1.00 −0.91 295.65 1257.20 ± 1.00 −2.69 07-che-11) 373.15 1206.00 ± 1.00 −1.00 288.15 1264.40 ± 0.50 −0.46 35-tim/hen( ) 393.15 1192.00 ± 1.02 −0.91 293.15 1261.31 ± 0.50 −0.24 35-tim/hen( ) 413.15 1178.00 ± 1.04 −0.63 303.15 1255.09 ± 0.50 0.20 35-tim/hen( ) 433.15 1164.00 ± 1.06 −0.16 298.15 1258.50 ± 0.50 0.27 37-alb( ) 453.15 1150.00 ± 1.08 0.48 298.15 1258.30 ± 0.60 0.07 473.15 1135.00 ± 1.10 0.31 42-bri/rin(∆) 303.15 1254.90 ± 0.60 0.01 493.15 1120.00 ± 1.12 0.33 42-bri/rin(∆) 313.15 1248.60 ± 0.60 0.41 513.15 1105.00 ± 1.14 0.53 42-bri/rin(∆) 323.15 1242.20 ± 0.60 0.76 533.15 1089.00 ± 1.16 −0.09 42-bri/rin(∆) 333.15 1235.80 ± 0.60 1.16 553.15 1068.00 ± 1.18 −5.53 42-bri/rin(∆) 296.75 1258.60 ± 0.50 −0.56 46-par/wes(✕ ) 293.15 1261.90 ± 0.60 0.35 293.15 1262.00 ± 1.00 0.45 58-cos/bow(✕ ) 298.15 1258.10 ± 0.80 −0.13 313.15 1249.00 ± 1.00 0.81 58-cos/bow(✕ )

1)

Ref. (Symbol in Fig. 1) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow(✕ ) 58-cos/bow1) 68-ano(∇) 69-ver/lau(◆)

Not included in Fig. 1.

Further references: [1885-sto, 1891-gla, 17-jae-1, 32-bri-2, 35-but/ram-1, 36-ern/wat, 70-che/tho, 77-cam/sch].

cont.

Landolt-Börnstein New Series IV/8G

358

4 Triols

ρ

ρ

1,2,3-Propanetriol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

280.00 290.00 293.15 298.15 300.00 310.00 320.00 330.00 340.00 350.00

ρ ± σ fit kg ⋅ m−3 1270.23 ± 0.95 1263.64 ± 0.94 1261.55 ± 0.93 1258.23 ± 0.93 1256.99 ± 0.92 1250.30 ± 0.91 1243.57 ± 0.91 1236.79 ± 0.90 1229.96 ± 0.90 1223.09 ± 0.89

T K

360.00 370.00 380.00 390.00 400.00 410.00 420.00 430.00 440.00 450.00

ρ ± σ fit kg ⋅ m−3 1216.17 ± 0.90 1209.21 ± 0.91 1202.19 ± 0.92 1195.14 ± 0.93 1188.04 ± 0.94 1180.89 ± 0.95 1173.69 ± 0.96 1166.45 ± 0.98 1159.17 ± 1.00 1151.84 ± 1.03

T K

460.00 470.00 480.00 490.00 500.00 510.00 520.00 530.00 540.00

ρ ± σ fit kg ⋅ m−3 1144.46 ± 1.07 1137.03 ± 1.12 1129.56 ± 1.18 1122.05 ± 1.27 1114.49 ± 1.37 1106.88 ± 1.48 1099.23 ± 1.62 1091.53 ± 1.78 1083.78 ± 1.96

Landolt-Börnstein New Series IV/8G

4 Triols 1,2,4-Butanetriol

[3068-00-6]

359 C4H10O3

MW = 106.12

825

C5H12O3

MW = 120.15

826

C6H14O3

MW = 134.18

827

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 62-mel 1184.0 ± 2.0

1,3,5-Pentanetriol

[4328-94-3]

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. −3 K kg ⋅ m 298.15 48-adk/bil 1103.6 ± 1.0

1,2,6-Hexanetriol

[106-69-4]

Table 1. Coefficients of the polynomial expansion equation. Standard deviations (see introduction): σc,w = 5.4613 · 10−2 (combined temperature ranges, weighted), σc,uw = 1.4472 · 10−2 (combined temperature ranges, unweighted). T = 293.15 to 343.15 K ρ = A + BT + CT 2 + DT 3 + … 1.26157 · 103 −4.84437 · 10−1 −1.92931 · 10−4

Coefficient A B C

Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc Ref. (Symbol ρexp ± 2σ est ρexp ± 2σ est T T in Fig. 1) in Fig. 1) kg ⋅ m−3 kg ⋅ m−3 K K kg ⋅ m−3 kg ⋅ m−3 293.15 1103.00 ± 1.00 0.02 96-gri/zhu( ) 323.15 1084.90 ± 1.00 0.02 96-gri/zhu( ) 303.15 1097.00 ± 1.00 0.01 96-gri/zhu( ) 333.15 1078.80 ± 1.00 0.03 96-gri/zhu( ) 313.15 1090.90 ± 1.00 −0.05 96-gri/zhu( ) 343.15 1072.60 ± 1.00 −0.02 96-gri/zhu( )

Table 3. Recommended values (fit to the reliable experimental values according to the equations ρ = A + BT + CT 2 + DT 3 + … or ρ = [1 + 1.75(1 − T/Tc)1/3 + 0.75(1 − T/Tc)][ρc + A(Tc −T ) + B(Tc − T )2 + C(Tc − T )3 + D(Tc − T )4] ). T K

290.00 293.15 298.15

ρ ± σ fit kg ⋅ m−3 1104.86 ± 1.38 1102.98 ± 1.29 1099.99 ± 1.16

T K

300.00 310.00 320.00

ρ ± σ fit kg ⋅ m−3 1098.88 ± 1.12 1092.86 ± 0.94 1086.80 ± 0.85

T K

330.00 340.00 350.00

ρ ± σ fit kg ⋅ m−3 1080.70 ± 0.91 1074.56 ± 1.20 1068.39 ± 1.83 cont.

Landolt-Börnstein New Series IV/8G

360

4 Triols

ρ

ρ

1,2,6-Hexanetriol (cont.)

Fig. 1. The symbols show the deviation of the calculated from the experimental values from Table 2. The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. (Error bars smaller than the symbols are omitted for clarity of the figure.)

1,3,6-Hexanetriol

[18990-98-2]

C6H14O3

MW = 134.18

828

C7H16O3

MW = 148.2

829

Table 1. Experimental value with uncertainty. ρexp ± 2σ est T Ref. K kg ⋅ m−3 293.15 1104.1 ± 10.0 62-nik/vor

1,4,7-Heptanetriol

[3920-53-4]

Table 1. Fit with estimated B coefficient for 2 accepted points. Deviation σw = 1.260. Coefficient ρ = A + BT A 1259.98 B −0.640 cont.

Landolt-Börnstein New Series IV/8G

4 Triols Table 2. Experimental values with uncertainties and deviation from calculated values. T K 291.00 273.00

ρexp ± 2σ est −3

kg ⋅ m

1075.0 ± 3.0 1084.0 ± 3.0

ρexp − ρcalc kg ⋅ m

1.26 −1.26

Table 3. Recommended values. ρexp ± 2σ est T K kg ⋅ m−3 270.00 1087.2 ± 3.2 280.00 1080.8 ± 3.0 290.00 1074.4 ± 3.1 293.15 1072.4 ± 3.2 298.15 1069.2 ± 3.4

Landolt-Börnstein New Series IV/8G

Ref.

−3

18-ham 18-ham

361

References

363

References Reference codes are those used in the TRC SOURCE database. A reference code consists of the year prior to 1900, or the last two digits of the year after 1899, the first three letters of the first author , the first three letters of the second author. An additional sequence number is used when more than one reference in the database has an identical code. 1811-bra 1848-kop 1854-kop 1857-wur-1 1859-wur 1863-gla/dal 1864-lan 1864-wur 1865-men 1869-dup/pag 1869-lie 1869-zin 1870-gie 1871-lie/ros 1871-lie/ros-3 1871-ros 1872-but 1872-lin/von 1872-lin/von-2 1872-pie/puc 1873-fri/sil 1874-reb-1 1874-reb-2 1875-fla 1875-lie 1875-lie/vol 1875-wag/say 1875-wag/say-1 1876-bal 1876-dec 1876-lin 1876-mun 1877-cro 1877-cro-1 1877-lie/jan 1878-roh 1878-win 1878-wis 1879-bel 1879-bru 1879-car 1879-pav 1880-bru-1 1880-bru-3 1880-pry 1880-tho Landolt-Börnstein New Series IV/8G

Brande, W. T.; Philos. Trans. R. Soc. London 101 (1811) 337. Kopp, H.; Justus Liebigs Ann. Chem. 64 (1848) 212. Kopp, H.; Justus Liebigs Ann. Chem. 92 (1854) 1. Wurtz, A.; C. R. Hebd. Seances Acad. Sci. 45 (1857) 306. Wurtz, A.; Ann. Chim. Phys. 55 (1859) 400. Gladstone, J. H.; Dale, T. P.; Philos. Trans. R. Soc. London 153 (1863) 317. Landolt, H.; Ann. Phys. (Leipzig) 122 (1864) 545. Wurtz, A.; Ann. Chim. Phys. 3 (1864) 129. Mendeleev, D.; Z. Chem. 8 (1865) 257. Dupre; Page; Philos. Trans. R. Soc. London 159 (1869) 591. Lieben, A.; Justus Liebigs Ann. Chem. 150 (1869) 87. Zincke, T.; Justus Liebigs Ann. Chem. 152 (1869) 1. Giesecke, A.; Z. Chem. 13 (1870) 430. Lieben, A.; Rossi, A.; Justus Liebigs Ann. Chem. 158 (1871) 137. Lieben, A.; Rossi, A.; Justus Liebigs Ann. Chem. 159 (1871) 70. Rossi, A.; Justus Liebigs Ann. Chem. 159 (1871) 79. Butlerov, A.; Justus Liebigs Ann. Chem. 162 (1872) 228. Linnemann, E.; von Zotta, V.; Justus Liebigs Ann. Chem. 161 (1872) 15. Linnemann, E.; von Zotta, V.; Justus Liebigs Ann. Chem. 162 (1872) 3. Pierre, J. -I.; Puchot, E.; Justus Liebigs Ann. Chem. 163 (1872) 253. Friedel, C.; Silva, R. D.; C. R. Hebd. Seances Acad. Sci. 76 (1873) 226. Reboul, C. E.; C. R. Hebd. Seances Acad. Sci. 79 (1874) 169. Reboul, C. E.; Jahresbericht fur Chem. (1874) 336. Flavitsky, F.; Justus Liebigs Ann. Chem. 179 (1875) 340. Lieben, A.; Chem. Ber. 8 (1875) 1017. Lieben, A.; Volker, O.; Chem. Ber. 8 (1875) 1019. Wagner, G.; Saytzeff, A.; Justus Liebigs Ann. Chem. 175 (1875) 351. Wagner, G.; Saytzeff, A.; Justus Liebigs Ann. Chem. 179 (1875) 302. Balbiano, L.; Gazz. Chim. Ital. 6 (1876) 229. De Cininck, M. W. O.; Bull. Soc. Chim. Fr. 25 (1876) 7. Linnemann, E.; Chem. Ber. 9 (1876) 924. Munch, R.; Justus Liebigs Ann. Chem. 180 (1876) 327. Cross, C. J.; Justus Liebigs Ann. Chem. 189 (1877) 1. Cross, C. J.; Chem. Ber. 10 (1877) 1601. Lieben, A.; Janecek, G.; Justus Liebigs Ann. Chem. 187 (1877) 126. Rohn, W.; Justus Liebigs Ann. Chem. 190 (1878) 305. Winogradow, W.; Justus Liebigs Ann. Chem. 191 (1878) 125. Wischnegradsky, A.; Justus Liebigs Ann. Chem. 190 (1878) 328. Belohoubek, A.; Chem. Ber. 12 (1879) 1872. Bruhl, J. W.; Justus Liebigs Ann. Chem. 200 (1879) 139. Carleton-Williams, W.; J. Chem. Soc. 35 (1879) 125. Pavlov, D.; Justus Liebigs Ann. Chem. 196 (1879) 122. Bruhl, J. W.; Justus Liebigs Ann. Chem. 203 (1880) 1. Bruhl, J. W.; Justus Liebigs Ann. Chem. 200 (1880) 139. Prytz, K.; Ann. Phys. (Leipzig) 11 (1880) 104. Thorpe, T. E.; J. Chem. Soc. 37 (1880) 141.

364 1881-ber 1881-nac/pag 1881-pri/han 1882-sch-1 1882-zan 1883-fre 1883-kra 1883-lie/zei 1883-sch-3 1883-wis 1884-gla 1884-kra 1884-per 1884-sch-6 1884-zan 1885-sto 1886-gar 1886-hen 1886-kra 1886-tra 1887-ram/you 1887-ref 1888-ket 1889-lip 1889-ram/you 1890-dek 1890-gar 1891-gla 1891-gri/paw 1891-jah 1891-pol 1891-sch/kos 1892-lan/jah 1892-sch-1 1893-eyk 1893-eyk-1 1893-ram/shi-3 1893-tho/jon 1894-jah/mol 1894-sch 1895-eyk 1896-zel/kra 1897-tho 1897-zec 1898-kah 1898-lou 1898-roh 00-car-1 00-loo 00-ste 01-def-1 01-gue

References Berthelot, M.; Ann. Chim. Phys. 23 (1881) 176. Naccari, A.; Pagliani, S.; Atti R. Accad. Sci. Torino, Cl. Sci. Fis. Mat. Nat. 16 (1881) 407. Pribram, A.; Handl, B.; Monatsh. Chem. 2 (1881) 643. Schiff, R.; Chem. Ber. 15 (1882) 2965. Zander, A.; Justus Liebigs Ann. Chem. 214 (1882) 138. Frentzel, J.; Chem. Ber. 16 (1883) 743. Krafft, F.; Ber. Dtsch. Chem. Ges. 16 (1883) 1714. Lieben, A.; Zeisel, B.; Monatsh. Chem. 4 (1883) 10. Schiff, R.; Justus Liebigs Ann. Chem. 220 (1883) 71. Wislicenus, J.; Justus Liebigs Ann. Chem. 219 (1883) 307. Gladstone, J. H.; J. Chem. Soc., Trans. 45 (1884) 241. Krafft, F.; Chem. Ber. 17 (1884) 1627. Perkin, W. H. ; J. Chem. Soc. 45 (1884) 421. Schiff, R.; Justus Liebigs Ann. Chem. 223 (1884) 47. Zander, A.; Justus Liebigs Ann. Chem. 224 (1884) 56. Stohmann, F.; J. Prakt. Chem. 31 (1885) 273. Gartenmeister, R.; Justus Liebigs Ann. Chem. 233 (1886) 249. Henninger, A.; Ann. Chim. Phys. 7 (1886) 209. Krafft, F.; Chem. Ber. 19 (1886) 2218. Traube, J.; Chem. Ber. 19 (1886) 871. Ramsay, W.; Young, S.; Philos. Trans. R. Soc. London, A 178 (1887) 313. Reformatsky, A.; J. Prakt. Chem. 36 (1887) 340. Ketteler, E.; Ann. Phys. (Leipzig) 33 (1888) 506. Lipp, A.; Chem. Ber. 22 (1889) 2567. Ramsay, W.; Young, S.; Philos. Trans. R. Soc. London, A 180 (1889) 137. Dekkers, P. J.; Recl. Trav. Chim. Pays-Bas 9 (1890) 92. Gartenmeister, R.; Z. Phys. Chem., Stoechiom. Verwandtschaftsl. 6 (1890) 524. Gladstone, J. H.; J. Chem. Soc. 59 (1891) 290. Grigorwitsch, A.; Pawlow, B.; Zh. Russ. Fiz.-Khim. O-va. 23 (1891) 172. Jahn, H.; Ann. Phys. (Leipzig) 43 (1891) 280. Poletaeff, G.; Chem. Ber. 24 (1891) 1308. Schall, C.; Kossakowsky, L.; Z. Phys. Chem., Stoechiom. Verwandtschaftsl. 8 (1891) 241. Landolt, H.; Jahn, H.; Z. Phys. Chem., Stoechiom. Verwandtschaftsl. 10 (1892) 289. Schuett, F.; Z. Phys. Chem., Stoechiom. Verwandtschaftsl. 9 (1892) 349. Eykman, J. F.; Recl. Trav. Chim. Pays-Bas 12 (1893) 157. Eykman, J. F.; Recl. Trav. Chim. Pays-Bas 12 (1893) 268. Ramsay, W.; Shields, J.; Z. Phys. Chem., Stoechiom. Verwandtschaftsl. 12 (1893) 433. Thorpe, T. E.; Jones, L. M.; J. Chem. Soc., Trans. 63 (1893) 273. Jahn, H.; Moller, G.; Z. Phys. Chem. (Leipzig) 13 (1894) 385. Schlamp, A.; Z. Phys. Chem. (Leipzig) 14 (1894) 272. Eykman, J. F.; Recl. Trav. Chim. Pays-Bas 14 (1895) 185. Zelinskii, N. D.; Krapiwin, S.; Z. Phys. Chem. (Leipzig) 21 (1896) 35. Thorpe, T. E.; J. Chem. Soc., Trans. 71 (1897) 920. Zecchini, F.; Gazz. Chim. Ital. 27 (1897) 358. Kahlbaum, G. W. A.; Z. Phys. Chem., Stoechiom. Verwandtschaftsl. 26 (1898) 577. Louguinine, W.; Ann. Chim. Phys. 13 (1898) 289. Rohland, P.; Z. Anorg. Chem. 18 (1898) 327. Carleton-Williams, W.; J. Chem. Soc. 77 (1900) 125. Loomis, E. H.; Z. Phys. Chem., Stoechiom. Verwandtschaftsl. 32 (1900) 578. Stephan, K.; J. Prakt. Chem. 62 (1900) 523. De Forcrand, M.; C. R. Hebd. Seances Acad. Sci. 132 (1901) 569. Guerbet, M.; C. R. Hebd. Seances Acad. Sci. 132 (1901) 207.

Landolt-Börnstein New Series IV/8G

References 01-gue-1 01-ham 01-mar/mck 01-rud 01-zel/zel 02-dud/lem 02-gri/tis 02-gue 02-kon 02-you 02-you/for 03-bla/gue 03-car/cop 03-tho/man 04-bou/bla 04-bou/bla-2 04-bru/sch 04-cri 04-dun 04-gri 04-gri-1 04-ham 04-kon 05-dun 05-win 06-bou/loc 06-car/fer 06-kla/nor 06-kon/mil 06-mal-1 06-mus 06-van 06-wal-1 07-che 07-che-1 07-dun/tho 07-fav/sok-3 07-fou/tif 07-kut 07-pic/ken 07-sok 07-tim 07-wal-4 08-and 08-bue 08-bue-1 08-dor/dvo 08-dor/rak 08-dun/stu 08-get 08-gyr 08-har

Landolt-Börnstein New Series IV/8G

365

Guerbet, M.; C. R. Hebd. Seances Acad. Sci. 133 (1901) 1220. Hamonet, J.; C. R. Hebd. Seances Acad. Sci. 132 (1901) 631. Marckwald, W.; McKenzie, A.; Chem. Ber. 34 (1901) 485. Rudolphi, M.; Z. Phys. Chem. (Leipzig) 37 (1901) 426. Zelinskii, N. D.; Zelikov, J.; Ber. Dtsch. Chem. Ges. 34 (1901) 2856. Duden, P.; Lemme, R.; Ber. Dtsch. Chem. Ges. 35 (1902) 1335. Grignard, V.; Tissier, L.; C. R. Hebd. Seances Acad. Sci. 134 (1902) 107. Guerbet, M.; C. R. Hebd. Seances Acad. Sci. 135 (1902) 172. Konovalov, M. I.; Zh. Russ. Fiz.-Khim. O-va. 34 (1902) 26. Young, S.; J. Chem. Soc. 81 (1902) 707. Young, S.; Fortey, E. C.; J. Chem. Soc. 81 (1902) 717. Blaise, E. E.; Guerin; Bull. Soc. Chim. Fr. 29 (1903) 1202. Carrara, G.; Coppadoro, A.; Gazz. Chim. Ital. 33 (1903) 329. Thoms, H.; Mannich, C.; Chem. Ber. 36 (1903) 2544. Bouveault, L.; Blanc, G.; Bull. Soc. Chim. Fr. 31 (1904) 1203. Bouveault, L.; Blanc, G.; Bull. Soc. Chim. Fr. 31 (1904) 748. Bruhl, J. W.; Schroder, H. ; Z. Phys. Chem. (Leipzig) 50 (1904) 1. Crismer, L.; Bull. Soc. Chim. Belg. 18 (1904) 18. Dunstan, A. E.; Z. Phys. Chem., Stoechiom. Verwandtschaftsl. 49 (1904) 590. Grignard, V.; Bull. Soc. Chim. Fr. 31 (1904) 751. Grignard, V.; C. R. Hebd. Seances Acad. Sci. 138 (1904) 152. Hamonet, J. L.; C. R. Hebd. Seances Acad. Sci. 139 (1904) 59. Konovalov, M. I.; Zh. Russ. Fiz.-Khim. O-va. 36 (1904) 228. Dunstan, A. E.; Z. Phys. Chem. (Leipzig) 51 (1905) 732. Winkler, L. W.; Ber. Dtsch. Chem. Ges. 38 (1905) 3612. Bouveault, L.; Locquin, R.; Bull. Soc. Chim. Fr. 35 (1906) 646. Carrara, G.; Ferrari, G.; Gazz. Chim. Ital. 36 (1906) 1419. Klason, P.; Norlin, E.; Ark. Kemi, Mineral. Geol. 2(24) (1906) 1. Konovalov, D.; Miller, E. F.; Timchenko; Zh. Russ. Fiz.-Khim. O-va. 38 (1906) 447. Malengraeu, F.; Bull. Cl. Sci. Acad. R. Belg. (1906) 796. Muset, J.; Bull. Cl. Sci. Acad. R. Belg. (1906) 775. Van Gysegem, J.; Bull. Cl. Sci. Acad. R. Belg. (1906) 692. Walden, P.; Z. Phys. Chem., Stoechiom. Verwandtschaftsl. 55 (1906) 207. Cheneveau, C.; Ann. Chim. Phys. 12 (1907) 145. Cheneveau, C.; Ann. Chim. Phys. 12 (1907) 289. Dunstan, A. E.; Thole, B. T.; Hunt, J. S.; J. Chem. Soc. 91 (1907) 1728. Favorskii, A.; Sokovnin, N.; Justus Liebigs Ann. Chem. 354 (1907) 364. Fourneau, A. C.; Tiffeneau, D.; C. R. Hebd. Seances Acad. Sci. 145 (1907) 437. Kutscherov, L.; Ann. 354 (1907) 376. Pickard, R. H.; Kenyon, J.; J. Chem. Soc. 91 (1907) 2058. Sokovnin, N.; Justus Liebigs Ann. Chem. 354 (1907) 364. Timmermans, J.; Bull. Soc. Chim. Belg. 21 (1907) 395. Walden, P.; Z. Phys. Chem., Stoechiom. Verwandtschaftsl. 59 (1907) 304. Andrew, L. W.; J. Am. Chem. Soc. 30 (1908) 353. Buelens, A.; Bull. Cl. Sci. Acad. R. Belg. (1908) 921. Buelens, A.; Recl. Trav. Chim. Pays-Bas 28 (1908) 113. Doroshevskii, A. G.; Dvorzhanchik, Z.; Zh. Russ. Fiz.-Khim. O-va., Chast Khim. 40 (1908) 908. Doroshevskii, A. G.; Rakovskii, A. V.; Zh. Russ. Fiz.-Khim. O-va., Chast Khim. 40 (1908) 860. Dunstan, A. E.; Stubbs, J. A.; J. Chem. Soc., Trans. 93 (1908) 1919. Getman, F. H.; J. Am. Chem. Soc. 30 (1908) 1077. Gyr, J.; Ber. Dtsch. Chem. Ges. 41 (1908) 4332. Hardin, D.; J. Chim. Phys. Phys.-Chim. Biol. 6 (1908) 584.

366 08-ric/mat 08-zel/prz 09-bod/tab 09-cla 09-dor 09-dor/roz 09-fal-1 09-gue 09-hen 09-hol/sag 09-kho 09-lem 09-lem-1 09-mas 09-sch-1 09-sch-2 10-daw 10-dor/pol 10-dor/pol-1 10-fon 10-fre 10-hal/las 10-pol 10-ric 10-tho 10-tim 11-del 11-dor 11-dor-1 11-kai 11-pic/ken 11-sch 11-wal 11-zel/arj 12-bje 12-gue 12-gue-1 12-gue-2 12-ipa 12-kor 12-mal 12-mic 12-osb/mck 12-ost 12-pic/ken 12-sch-1 12-sch-2 12-sch-3 12-tim 12-tim-1 12-tyr

References Richards, T. W.; Mathews, J. H.; J. Am. Chem. Soc. 30 (1908) 8. Zelinskii, N. D.; Przheval'skii, E. C.; Zh. Russ. Fiz.-Khim. O-va., Chast Khim. 40 (1908) 1105. Bodroux, F.; Taboury, F.; Bull. Soc. Chim. Fr. 5 (1909) 812. Claessens, F.; Bull. Soc. Chim. Fr. 5 (1909) 113. Doroshevskii, A. G.; Zh. Russ. Fiz.-Khim. O-va., Chast Khim. 41 (1909) 958. Doroshevskii, A. G.; Rozhdestvenskii, M. S.; Zh. Russ. Fiz.-Khim. O-va., Chast Khim. 41 (1909) 1428. Falk, K. G.; J. Am. Chem. Soc. 31 (1909) 86. Guerbet, M.; C. R. Hebd. Seances Acad. Sci. 149 (1909) 129. Henry, L; Recl. Trav. Chim. Pays-Bas 28 (1909) 444. Holmes, J.; Sageman, P. J.; J. Chem. Soc. 95 (1909) 1919. Khonin, G. V.; Zh. Russ. Fiz.-Khim. O-va., Chast Khim. 41 (1909) 327. Lemaire, J.; Bull. Cl. Sci. Acad. R. Belg. (1909) 83. Lemaire, J.; Recl. Trav. Chim. Pays-Bas 29 (1909) 22. Masson, H.; C. R. Hebd. Seances Acad. Sci. 149 (1909) 630. Schultz, G.; Ber. Dtsch. Chem. Ges. 42 (1909) 3609. Schwers, M. F.; Recl. Trav. Chim. Pays-Bas Belg. 28 (1909) 42. Dawson, H. M.; J. Chem. Soc. 97 (1910) 1041. Doroshevskii, A.; Polansky, E.; Z. Phys. Chem., Stoechiom. Verwandtschaftsl. 73 (1910) 192. Doroshevskii, A. G.; Polyanskii, E. V.; Zh. Russ. Fiz.-Khim. O-va., Chast Khim. 42 (1910) 109. Fontein, F.; Z. Phys. Chem., Stoechiom. Verwandtschaftsl. 73 (1910) 212. Freylon, G.; Ann. Chim. (Paris) 20 (1910) 58. Haller, A.; Lassieur, A.; C. R. Hebd. Seances Acad. Sci. 151 (1910) 697. Polowzow, V.; Z. Phys. Chem. (Leipzig) 75 (1910) 513. Richard, A.; Ann. Chim. Phys. 21 (1910) 323. Thole, F. B.; J. Chem. Soc. 97 (1910) 2596. Timmermans, J.; Bull. Soc. Chim. Belg. 24 (1910) 244. De Leeuw, H. L.; Z. Phys. Chem., Stoechiom. Verwandtschaftsl. 77 (1911) 284. Doroshevskii, A. G.; Zh. Russ. Fiz.-Khim. O-va., Chast Khim. 43 (1911) 46. Doroshevskii, A. G.; Zh. Russ. Fiz.-Khim. O-va., Chast Khim. 43 (1911) 66. Kailan, A.; Ber. Dtsch. Chem. Ges. 44 (1911) 2881. Pickard, R. H.; Kenyon, J.; J. Chem. Soc. 99 (1911) 45. Schwers, F.; J. Chim. Phys. Phys.-Chim. Biol. 9 (1911) 15. Wallach, O.; Justus Liebigs Ann. Chem. 381 (1911) 51. Zelinskii, N. D.; Arjedinoff; J. Prakt. Chem. 84 (1911) 543. Bjelouss, E.; Ber. Dtsch. Chem. Ges. 45 (1912) 625. Guerbet, M.; Bull. Soc. Chim. Fr. 11 (1912) 276. Guerbet, M.; Bull. Soc. Chim. Fr. 11 (1912) 533. Guerbet, M.; C. R. Hebd. Seances Acad. Sci. 154 (1912) 1357. Ipatieff, W.; Chem. Ber. 45 (1912) 3218. Korber, F.; Ann. Phys. (Leipzig) 37 (1912) 1014. Malosse, H.; C. R. Hebd. Seances Acad. Sci. 154 (1912) 1697. Michiels, L.; Bull. Cl. Sci. Acad. R. Belg. (1912) 10. Osborne, N. S.; McKelvy, E. C.; Bearce, H. W.; J. Wash. Acad. Sci. 2 (1912) 95. Ostling, G. J.; J. Chem. Soc. 101 (1912) 457. Pickard, R. H.; Kenyon, J.; J. Chem. Soc. 101 (1912) 620. Schwers, F.; Bull. Cl. Sci. Acad. R. Belg. (1912) 610. Schwers, F.; Bull. Cl. Sci. Acad. R. Belg. (1912) 719. Schwers, F.; J. Chem. Soc., Trans. 101 (1912) 1889. Timmermans, J.; Bull. Soc. Chim. Belg. 26 (1912) 205. Timmermans, J.; Sci. Proc. R. Dublin Soc. 13 (1912) 310. Tyrer, D.; J. Chem. Soc., Trans. 101 (1912) 1104.

Landolt-Börnstein New Series IV/8G

References 12-wad/mer 12-wre 13-atk/wal 13-bri-1 13-dup 13-fav 13-gor 13-har 13-kis-3 13-mer 13-muc 13-osb/mck 13-pic/ken 13-rob/acr 13-rom 13-ste 13-tho 14-eng/tur 14-gas 14-hal 14-kre/mei 14-lon 14-low 14-mer/tur 14-mur/amo 14-smi 14-tyr 14-vav 14-wal-1 14-wor 15-pea 15-pri 15-ric/coo 15-sch-1 15-wal-3 16-har-2 16-lev/all 16-ric/shi 16-sei/alt 16-wil/bru 16-wro/rei 17-jae 17-jae-1 18-abd/eic 18-bro/hum 18-ham 18-her-2 18-kar 18-lev/tay 19-beh 19-eyk 19-ort/jon

Landolt-Börnstein New Series IV/8G

Wade, J. W.; Merriman, R. W.; J. Chem. Soc. 101 (1912) 2429. Wrewski, M. S.; Z. Phys. Chem. (Leipzig) 81 (1912) 20. Atkins, W. R. G.; Wallace, T. A.; J. Chem. Soc., Trans. 103 (1913) 1461. Bridgman, P. W.; Proc. Am. Acad. Arts Sci. 49 (1913) 3. Dupont, G.; Ann. Chim. Phys. 30 (1913) 485. Favorskii, A.; J. Prakt. Chem. 88 (1913) 641. Gorskii, A.; Zh. Russ. Fiz.-Khim. O-va., Chast Khim. 45 (1913) 167. Hardy, W. B.; Proc. R. Soc. London, A 88 (1913) 303. Kishner, N.; Zh. Russ. Fiz.-Khim. O-va., Chast Khim. 45 (1913) 973. Merriman, R. W.; J. Chem. Soc. 103 (1913) 628. Muchin, G.; Z. Electrochem. Angew. Phys. Chem. 19 (1913) 819. Osborne, N. S.; McKelvy, E. C.; Bearce, H. W.; Bur. Stand. (U. S.), Bull. 9 (1913) 327. Pickard, R. H.; Kenyon, J.; J. Chem. Soc. 103 (1913) 1923. Robertson, H. C.; Acree, S. F.; Am. Chem. J. 49 (1913) 474. Romanov, W.; Ann. Phys. (Leipzig) 40 (1913) 281. Stern, O.; Z. Phys. Chem., Stoechiom. Verwandtschaftsl. 81 (1913) 441. Thole, F. B.; J. Chem. Soc. 103 (1913) 19. English, S.; Turner, W. E. S.; J. Chem. Soc., Trans. 105 (1914) 1656. Gascard, A.; C. R. Hebd. Seances Acad. Sci. 159 (1914) 259. Halse, M. O.; J. Prakt. Chem. 89 (1914) 451. Kremann, R.; Meingast, R.; Gugl, F.; Monatsh. Chem. 35 (1914) 1235. Longinov, V.; Zh. Russ. Fiz.-Khim. O-va., Chast Khim. 46 (1914) 1084. Lowry, T. M.; J. Chem. Soc. 105 (1914) 81. Merry, E. W.; Turner, W. E. S.; J. Chem. Soc. 105 (1914) 748. Murat, M.; Amouroux, G.; Bull. Soc. Chim. Fr. 15 (1914) 159. Smith, C.; J. Chem. Soc., Trans. 105 (1914) 1703. Tyrer, D.; J. Chem. Soc., Trans. 105 (1914) 2534. Vavon, G.; Ann. Chim. (Paris) 1 (1914) 144. Wallach, O.; Justus Liebigs Ann. Chem. 408 (1914) 183. Worley, R. P.; J. Chem. Soc. 105 (1914) 260 Peacock, D. H.; J. Chem. Soc. 107 (1915) 1547. Price, T. W.; J. Chem. Soc. 107 (1915) 188. Richards, T. W.; Coombs, L. B.; J. Am. Chem. Soc. 37 (1915) 1656. Schwers, F.; Bull. Cl. Sci. Acad. R. Belg. (1915) 525. Wallach, O.; Justus Liebigs Ann. Chem. 408 (1915) 200. Hartung, E. J.; Trans. Faraday Soc. 12 (1916) 66. Levene, P. A.; Allen, C. H.; J. Biol. Chem. 27 (1916) 433. Richards, T. W.; Shipley, J. W.; J. Am. Chem. Soc. 38 (1916) 989. Seitz, W.; Alterthum, H.; Lechner, G.; Ann. Phys. (Leipzig) 49 (1916) 85. Willcox, M.; Brunel, R. F.; J. Am. Chem. Soc. 38 (1916) 1821. Wroth, B. B.; Reid, E. E.; J. Am. Chem. Soc. 38 (1916) 2316. Jaeger, F. M.; Z. Anorg. Allg. Chem. 101 (1917) 130. Jaeger, F. M.; Z. Anorg. Allg. Chem. 101 (1917) 1. Abderhalden, E.; Eichwald, E.; Chem. Ber. 51 (1918) 1312. Brooks, B. T.; Humphrey, I.; J. Am. Chem. Soc. 40 (1918) 822. Hamonet, J.; Ann. Chim. Phys. 10 (1918) 28. Herz, W.; Z. Anorg. Chem. 104 (1918) 47. Karvonen, A.; Ann. Acad. Sci. Fenn., Ser. A 10 (1918) 9. Levene, P. A.; Taylor, F. A.; J. Biol. Chem. 35 (1918) 281. Behal, A.; Bull. Soc. Chim. Fr. 25 (1919) 473. Eykman, J. F.; Natuurkd. Verh. Hollandsche Maatschappij Wet. Haarlem 8 (1919) 438. Orton, K. J. P.; Jones, D. C.; J. Chem. Soc. 115 (1919) 1194.

367

368 19-rei/ral 19-wil/hat 19-wil/sch 20-ric/dav 21-bar/bir 21-bru/cre 21-leb 21-ler 21-par/sim 21-rei/hic 22-bae 22-her/sch 22-lev/tay-1 22-mck/sim 22-mic 22-sch/reg 22-tim 22-tro 23-bru 23-clo/joh 23-kau/ada 23-moe-1 23-pop 23-rii 23-tim 23-vav/iva 23-von/kai 23-wil/smi 24-bou 24-bus-1 24-cha/deg 24-dan 24-dew/wec 24-lie 24-lon/mar 24-mar-1 24-mil 24-par/sch 24-pow 24-ter 25-deg 25-fai 25-fai-1 25-fav/zal 25-gro/kel 25-har/rai 25-hes/bap 25-lew 25-nor/ash 25-pal/con 25-par 25-par/kel

References Reilly, J.; Ralph, E. W.; Sci. Proc. R. Dublin Soc. 15 (1919) 597. Willstatter, R.; Hatt, D.; Justus Liebigs Ann. Chem. 418 (1919) 148. Willstatter, R.; Schuppli, O.; Mayer, E. W.; Justus Liebigs Ann. Chem. 418 (1919) 121 Richards, T. W.; Davis, H. S.; J. Am. Chem. Soc. 42 (1920) 1599. Barr, G.; Bircumshaw, L. L.; Aeron. Res. Comm. Rep. Mem. No. 746 (1921). Brunel, R. F.; Crenshaw, J. L.; Tobin, E.; J. Am. Chem. Soc. 43 (1921) 561. Lebo, R. B.; J. Am. Chem. Soc. 43 (1921) 1005. Leroide, J.; Ann. Chim. (Paris) 16 (1921) 354. Pariselle, M.; Simon, L. J.; C. R. Hebd. Seances Acad. Sci. 173 (1921) 86. Reilly, J.; Hickinbottom, W. J.; Sci. Proc. R. Dublin Soc. 16 (1921) 233. Baerts, F.; Bull. Soc. Chim. Belg. 31 (1922) 421. Herz, W.; Schuftan, P.; Z. Phys. Chem. (Leipzig) 101 (1922) 269. Levene, P. A.; Taylor, F. A.; J. Biol. Chem. 54 (1922) 351. McKelvy, E. C.; Simpson, D. H.; J. Am. Chem. Soc. 44 (1922) 105. Michels, A.; Arch. Neerl. Sci. Exactes Nat., Ser. 3A 6 (1922) 127. Schoorl, N.; Regenboden, A.; Recl. Trav. Chim. Pays-Bas 41 (1922) 1. Timmermans, J.; Arch. Neerl. Sci. Exactes Nat., Ser. 3A 6 (1922) 147. Tromp, S. T. J.; Recl. Trav. Chim. Pays-Bas 41 (1922) 278. Brunel, R. F.; J. Am. Chem. Soc. 45 (1923) 1334. Clough, W. W.; Johns, C. O.; Ind. Eng. Chem. 15 (1923) 1030. Kaufmann, W. E.; Adams, R.; J. Am. Chem. Soc. 45 (1923) 3029. Moesveld, A. L. Th.; Z. Phys. Chem., Stoechiom. Verwandtschaftsl. 105 (1923) 450. Popelier, J.; Bull. Soc. Chim. Belg. 32 (1923) 179. Riiber, C. N.; Z. Elektrochem. Angew. Phys. Chem. 29 (1923) 334. Timmermans, J.; Bull. Soc. Chim. Belg. 32 (1923) 299. Vavon, G.; Ivanoff, D.; C. R. Hebd. Seances Acad. Sci. 177 (1923) 453. Von Braun, J.; Kaiser, W.; Chem. Ber. 56 (1923) 2268. Willard, H. H.; Smith, G. F.; J. Am. Chem. Soc. 45 (1923) 286. Bourgou, A.; Bull. Soc. Chim. Belg. 33 (1924) 101. Busse, W.; Ann. Phys. (Leipzig) 75 (1924) 657. Chavanne, G.; De Graef, H.; Bull. Soc. Chim. Belg. 33 (1924) 366. Dancaster, E.; J. Chem. Soc. 125 (1924) 2036. Dewael, A.; Weckering, A.; Bull. Soc. Chim. Belg. 33 (1924) 495. Lievens, G.; Bull. Soc. Chim. Belg. 33 (1924) 122. Longinov, V.; Margoliss, E.; Bull. Soc. Chim. Fr. 35 (1924) 753. Mardles, E.; J. Chem. Soc. 125 (1924) 2244. Miller, C. C.; Proc. R. Soc. London, A 106 (1924) 724. Parks, G. S.; Schwenk, J. R.; J. Phys. Chem. 28 (1924) 720. Powell, S. G.; J. Am. Chem. Soc. 46 (1924) 2514. Terent'ev, A.; Bull. Soc. Chim. Fr. 35 (1924) 1145. De Graef, H.; Bull. Soc. Chim. Belg. 34 (1925) 427. Faillebin, M.; Ann. Chim. (Paris) 4 (1925) 156. Faillebin, M.; Ann. Chim. (Paris) 4 (1925) 410. Favorskii, A.; Zalesskii-Kibardine, T.; Bull. Soc. Chim. Fr. 37 (1925) 1227. Groh, Von J.; Kelp, I.; Z. Anorg. Allg. Chem. 147 (1925) 321. Hartley, H.; Raikes, H. R.; J. Chem. Soc. 127 (1925) 524. Hess, K.; Bappert, R.; Justus Liebigs Ann. Chem. 441 (1925) 137. Lewis, J. R.; J. Am. Chem. Soc. 47 (1925) 626. Norris, J. F.; Ashdown, A. A.; J. Am. Chem. Soc. 47 (1925) 837. Palmer, W. G.; Constable, F. H.; Proc. R. Soc. London, A 107 (1925) 255. Parks, G. S.; J. Am. Chem. Soc. 47 (1925) 338. Parks, G. S.; Kelley, K. K.; J. Am. Chem. Soc. 47 (1925) 2089.

Landolt-Börnstein New Series IV/8G

References 25-par/kel-1 25-per 25-pie/ada 25-rak 25-ric/cha 25-rii/soe 25-ter 25-tho/kah 25-vor/wal 26-bar 26-boe/bel 26-ewa/rai 26-gol/aar 26-han 26-mat 26-mun 26-nic 26-par/huf 26-pas/zam 26-ray 26-ris/hic 26-sch 26-sta 26-tay/rin 26-van 27-arb-2 27-bra/ada 27-cla/rob 27-del 27-kai/mel 27-krc/wil 27-mou/duf 27-nor/cor 27-nor/reu 27-par/cha 27-tri 27-tro/luk 27-ver/coo 28-dil/luc 28-esc 28-har-2 28-kro/see 28-llo/bro 28-mon 28-par/bar 28-par/kel 28-par/nel 28-pre-4 28-tim/mar 28-ven-1

Landolt-Börnstein New Series IV/8G

369

Parks, G. S.; Kelley, K. K.; J. Phys. Chem. 29 (1925) 727. Perrakis, N.; J. Chim. Phys. Phys.-Chim. Biol. 22 (1925) 280. Pierce, J. S.; Adams, R.; J. Am. Chem. Soc. 47 (1925) 1098. Rakshit, J. N.; Z. Elektrochem. Angew. Phys. Chem. 31 (1925) 320. Richards, T. W.; Chadwell, H. M.; J. Am. Chem. Soc. 47 (1925) 2283. Riiber, C. N.; Soerensen, T.; Thorkelsen, K.; Z. Elektrochem. Angew. Phys. Chem. 58 (1925) 964. Terent'ev, A.; Bull. Soc. Chim. Fr. 37 (1925) 1553. Thoms, H.; Kahre, H.; Arch. Pharm. Ber. Dtsch. Pharm. 263 (1925) 241. Vorlander, D.; Walter, R.; Z. Phys. Chem. (Leipzig) 118 (1925) 1. Barbaudy, J.; Bull. Soc. Chim. Fr. 39 (1926) 371. Boeseken, J.; Belinfante, A. H.; Recl. Trav. Chim. Pays-Bas 45 (1926) 914. Ewart, F. K.; Raikes, H. R.; J. Chem. Soc. (1926) 1907. Goldschmidt, H.; Aarflot, H.; Z. Phys. Chem., Stoechiom. Verwandtschaftsl. 122 (1926) 371. Hannotte, T.; Bull. Soc. Chim. Belg. 35 (1926) 86. Mathews, J. H.; J. Am. Chem. Soc. 48 (1926) 562. Munch, J. C.; J. Am. Chem. Soc. 48 (1926) 994. Nicolle, P.; Bull. Soc. Chim. Belg. 39 (1926) 55. Parks, G. S.; Huffman, H. M.; J. Am. Chem. Soc. 48 (1926) 2788. Pastureau, M.; Zamenhof, M. S.; Bull. Soc. Chim. Fr. 39 (1926) 1430. Rayne, G. J.; J. Soc. Chem. Ind., London, Trans. Commun. 45 (1926) 265. Rising, M. M.; Hicks, J. S.; J. Am. Chem. Soc. 48 (1926) 1929. Schmidt, G. C.; Z. Phys. Chem., Stoechiom. Verwandtschaftsl. 121 (1926) 221. Stas, J.; Bull. Soc. Chim. Belg. 35 (1926) 379. Taylor, C. A.; Rinkenbach, W. H.; Ind. Eng. Chem. 18 (1926) 676. Van Risseghem, H.; Bull. Soc. Chim. Belg. 35 (1926) 328. Arbusov, A. E.; Z. Phys. Chem., Stoechiom. Verwandtschaftsl. 131 (1927) 49. Bray, R. H.; Adams, R.; J. Am. Chem. Soc. 49 (1927) 2101. Clarke, J. T.; Robinson, R.; Smith, J. C.; J. Chem. Soc. (1927) 2647. De Lattre, G.; J. Chim. Phys. Phys.-Chim. Biol. 24 (1927) 289. Kailan, A.; Melkus, K.; Monatsh. Chem. 48 (1927) 9. Krchma, I. J.; Williams, J. W.; J. Am. Chem. Soc. 49 (1927) 2408. Moureu, C.; Dufraisse, C.; Ann. Chim. (Paris) 7 (1927) 1. Norris, J. F.; Cortese, F.; J. Am. Chem. Soc. 49 (1927) 2640. Norris, J. F.; Reuter, R.; J. Am. Chem. Soc. 49 (1927) 2624. Parks, G. S.; Chaffee, C. S.; J. Phys. Chem. 31 (1927) 439. Trickey, J. P.; Ind. Eng. Chem. 19 (1927) 643. Tronov, B. V.; Lukanin, A. A.; Pavlinov, I. I.; Zh. Russ Fiz.-Khim. O-va., Chast Khim. 59 (1927) 1174. Verkade, P. E.; Coops, J.; Recl. Trav. Chim. Pays-Bas 46 (1927) 903. Dillon, R. T. ; Lucas, H. J. ; J. Am. Chem. Soc. 50 (1928) 1711. Escourrou, R.; Bull. Soc. Chim. Fr. 43 (1928) 1101. Harkins, W. D.; Z. Phys. Chem., Abt. A 139 (1928) 647. Krollpfeiffer, F.; Seebaum, H.; J. Prakt. Chem. 119 (1928) 131. Lloyd, E.; Brown, C. B.; Bonnell, D. G. R.; Jones, W. J.; J. Chem. Soc. (1928) 658. Mondain-Monval, P.; C. R. Hebd. Seances Acad. Sci. 187 (1928) 444. Parks, G. S.; Barton, B.; J. Am. Chem. Soc. 50 (1928) 24. Parks, G. S.; Kelley, K. K.; J. Phys. Chem. 32 (1928) 734. Parks, G. S.; Nelson, W. K.; J. Phys. Chem. 32 (1928) 61. Prevost, C.; Ann. Chim. (Paris) 10 (1928) 356. Timmermans, J.; Martin, F.; J. Chim. Phys. Phys.-Chim. Biol. 25 (1928) 411. Venus-Danilova, E. D.; Bull. Soc. Chim. Fr. 43 (1928) 582.

370 29-ber 29-ber/mie 29-ber/reu 29-con/bla 29-edg/cal 29-ham/and 29-jon 29-kel 29-kel-1 29-kel-3 29-kir/ric 29-lev/mik 29-luc 29-mah/das 29-pre 29-sim 29-smy/sto 29-swa 29-tim/hen 30-bil/fis-1 30-bin/dar 30-bin/for 30-dav/dix 30-err/she 30-fro 30-mon 30-rak/fro 30-she 30-tim/hen 30-van 30-wal/ros 31-bea/mcv 31-chu/mar 31-def 31-deg 31-del 31-fio/gin 31-hom 31-lev/mar-1 31-lev/mar-2 31-lev/mar-3 31-lev/mar-4 31-lev/mar-5 31-lun/bje 31-pow/sec 31-smy/dor-1 31-smy/wal 31-sto/hul 31-ton/ueh 31-zaa 32-boe/wil 32-bri-2

References Berner, E.; Z. Phys. Chem., Abt. A 141 (1929) 91. Bergmann, M.; Miekeley, A.; Lippmann; Ber. Dtsch. Chem. Ges. A 62 (1929) 1467. Berlin, E.; Reuter, R.; Kolloid-Z. 47 (1929) 251. Conant, J. B.; Blatt, A. H.; J. Am. Chem. Soc. 51 (1929) 1227. Edgar, G.; Calingaert, G.; Marker, R. E.; J. Am. Chem. Soc. 51 (1929) 1483. Hammick, D. L.; Andrew, L. W.; J. Chem. Soc. (1929) 754. Jones, D. C.; J. Chem. Soc. (1929) 799. Kelley, K. K.; J. Am. Chem. Soc. 51 (1929) 1145. Kelley, K. K.; J. Am. Chem. Soc. 51 (1929) 180. Kelley, K. K.; J. Am. Chem. Soc. 51 (1929) 779. Kirner, W. R.; Richter, G. H.; J. Am. Chem. Soc. 51 (1929) 2505. Levene, P. A.; Mikeska, L. A.; J. Biol. Chem. 84 (1929) 571. Lucas, H. J. ; J. Am. Chem. Soc. 51 (1929) 248. Mahanti, P. C.; Das-Gupta, R. N.; Indian J. Phys. 3 (1929) 467. Prentiss, S. W.; J. Am. Chem. Soc. 51 (1929) 2825. Simon, I.; Bull. Soc. Chim. Belg. 38 (1929) 47. Smyth, C. P.; Stoops, W. N.; J. Am. Chem. Soc. 51 (1929) 3312. Swarts, F.; Bull. Soc. Chim. Belg. 38 (1929) 99. Timmermans, J.; Hennaut-Roland, M.; An. R. Soc. Esp. Fis. Quim. 27 (1929) 460 Biltz, W.; Fischer, W.; Wunnenberg, E.; Z. Phys. Chem., Abt. A 151 (1930) 13. Bingham, E. C.; Darrall, L. B.; J. Rheol. (Easton, Pa.) 1 (1930) 174. Bingham, E. C.; Fornwalt, H. J.; J. Rheol. (N. Y.) 1 (1930) 372. Davies, W. C.; Dixon, R. S.; Jones, W. J.; J. Chem. Soc. (1930) 468. Errera, J.; Sherrill, M. L.; J. Am. Chem. Soc. 52 (1930) 1993. Frost, A. V.; Tr. Inst. Chist. Khim. Reakt. No. 9 (1930) 105. Montagne, M.; Ann. Chim. (Paris) 13 (1930) 40. Rakovskii, A. V.; Frost, A. V.; Tr. Inst. Chist. Khim. Reakt. 9 (1930) 95. Sherrill, M. L.; J. Am. Chem. Soc. 52 (1930) 1982. Timmermans, J.; Hennaut-Roland, M.; J. Chim. Phys. Phys.-Chim. Biol. 27 (1930) 401. Van Risseghem, H.; Bull. Soc. Chim. Belg. 39 (1930) 369. Walbaum, H.; Rosenthal, A.; J. Prakt. Chem. 124 (1930) 63. Beare, W. G.; McVicar, G. A.; Ferguson, J. B.; J. Phys. Chem. 35 (1931) 1068. Chu, T. T.; Marvel, C. S.; J. Am. Chem. Soc. 53 (1931) 4449. Deffet, L.; Bull. Soc. Chim. Belg. 40 (1931) 385. De Graef, H.; Bull. Soc. Chim. Belg. 40 (1931) 315. Delcourt, Y.; Bull. Soc. Chim. Belg. 40 (1931) 284. Fiock, E. F.; Ginnings, D. C.; Holton, W. B.; J. Res. Natl. Bur. Stand. (U. S.) 6 (1931) 881. Homeyer, A. H.; Thesis, Pennsylvania State University, University Park, PA (1931) Levene, P. A.; Marker, R. E.; J. Biol. Chem. 91 (1931) 1931. Levene, P. A.; Marker, R. E.; J. Biol. Chem. 91 (1931) 405. Levene, P. A.; Marker, R. E.; J. Biol. Chem. 91 (1931) 687. Levene, P. A.; Marker, R. E.; J. Biol. Chem. 91 (1931) 761. Levene, P. A.; Marker, R. E.; J. Biol. Chem. 91 (1931) 77. Lund, H.; Bjerrum, J.; Ber. Dtsch. Chem. Ges. A 64 (1931) 210. Powell, S. G.; Secoy, C. H.; J. Am. Chem. Soc. 53 (1931) 765. Smyth, C. P.; Dornte, R. W.; J. Am. Chem. Soc. 53 (1931) 545. Smyth, C. P.; Walls, W. S.; J. Am. Chem. Soc. 53 (1931) 2115. Stockhardt, J. S.; Hull, C. M.; Ind. Eng. Chem. 23 (1931) 1438. Tonomura, T.; Uehara, K.; Bull. Chem. Soc. Jpn. 6 (1931) 118. Zaar, B.; J. Prakt. Chem. 132 (1931) 163. Boeseken, J.; Wildschut, A. J.; Recl. Trav. Chim. Pays-Bas 51 (1932) 168. Bridgman, P. W.; Proc. Am. Acad. Arts Sci. 67 (1932) 1.

Landolt-Börnstein New Series IV/8G

References 32-byl 32-con/adk 32-ell/rei 32-ern/lit 32-ess/cla 32-hun 32-kom/tal 32-les/wak 32-lev/mar 32-lon/kha 32-mor/har 32-pfa/pla 32-ros 32-sol/mol 32-swi/zma 32-tim/hen 33-ano 33-azi/bha 33-bin/ste 33-bri 33-but/tho 33-fav/naz 33-gin/her 33-har 33-hov/lan 33-huc/ack 33-kil 33-koz/koz 33-lev/mar-1 33-mey/tuo 33-nat/bac 33-nev/jat 33-pow/mur 33-ste 33-tre/wat 33-van 33-vos/con 33-whi/eve 33-whi/her 33-whi/hom 33-whi/hom-1 33-whi/kru 33-whi/lau 33-whi/wil 33-whi/woo 34-bur/adk 34-car/jon 34-cor/arc 34-gre 34-jac-5

Landolt-Börnstein New Series IV/8G

371

Bylewski, T.; Rocz. Chem. 12 (1932) 311. Connor, R.; Adkins, H.; J. Am. Chem. Soc. 54 (1932) 4678. Ellis, L. M.; Reid, E. E.; J. Am. Chem. Soc. 54 (1932) 1674. Ernst, R. C.; Litkenhous, E. E.; Spanyer, J. W.; J. Phys. Chem. 36 (1932) 842. Essex, H.; Clark, J. D.; J. Am. Chem. Soc. 54 (1932) 1290. Hunt, R.; Ind. Eng. Chem. 24 (1932) 361. Komppa, G.; Talvitie, Y.; J. Prakt. Chem. 135 (1932) 193. Lespieau, R.; Wakeman, R. L.; Bull. Soc. Chim. Fr. 51 (1932) 384. Levene, P. A.; Marker, R. E.; J. Biol. Chem. 95 (1932) 1. Longinov, V.; Khasanova, R.; Bull. Soc. Chim. Fr. 51 (1932) 636. Morgan, G. T.; Hardy, D. V. N.; Proctor, R. A.; J. Soc. Chem. Ind., London, Trans. Commun. 51 (1932) 1. Pfau, A. S.; Plattaner, Pl.; Helv. Chim. Acta 15 (1932) 1250. Rossini, F. D.; J. Res. Natl. Bur. Stand. (U. S.) 8 (1932) 119. Solana, L.; Moles, E.; An. R. Soc. Esp. Fis. Quim. 30 (1932) 886. Swietoslawski, W.; Zmaczynski, A. L.; Usakiewicz, J; C. R. Hebd. Seances Acad. Sci. 194 (1932) 357. Timmermans, J.; Hennaut-Roland, M.; J. Chim. Phys. Phys.-Chim. Biol. 29 (1932) 529. Schimmel & Co., Ann. Rep. (1933) . Azim, M. A.; Bhatnagar, S. S.; Mathur, R. N.; Philos. Mag. 16 (1933) 580. Bingham, E. C.; Stephens, R. A.; Physics (N. Y.) 4 (1933) 206. Bridgman, P. W.; Proc. Am. Acad. Arts Sci. 68 (1933) 1. Butler, J. A. V.; Thomson, D. W.; Maclennan, W. H.; J. Chem. Soc. (1933) 674. Favorskii, A.; Nazarov, I. N.; C. R. Hebd. Seances Acad. Sci. 196 (1933) 1229. Ginnings, P. M.; Herring, E.; Webb, B.; J. Am. Chem. Soc. 55 (1933) 875. Harris, L.; J. Am. Chem. Soc. 55 (1933) 1940. Hovorka, F.; Lankelma, H. P.; Naujoks, C. K.; J. Am. Chem. Soc. 55 (1933) 4820. Huckel, W.; Ackermann, P.; J. Prakt. Chem. 136 (1933) 15. Kilpi, S.; Z. Phys. Chem. (Leipzig) 166 (1933) 285. Kozakevich, P. P.; Kozakevich, N. S.; Z. Phys. Chem., Abt. A 166 (1933) 113. Levene, P. A.; Marker, R. E.; J. Biol. Chem. 103 (1933) 299. Meyer, A.; Tuot, M.; C. R. Hebd. Seances Acad. Sci. 196 (1933) 1231. Natta, G.; Baccaredda, M.; G. Chim. Ind. Appl. 15 (1933) 273. Nevgi, G. V.; Jatkar, S. K. K.; Indian J. Phys. 8 (1933) 397. Powell, S. G.; Murray, H. C.; Baldwin, M. M.; J. Am. Chem. Soc. 55 (1933) 1153. Stevens, P. G.; J. Am. Chem. Soc. 55 (1933) 4237. Trew, V. C. G.; Watkins, G. M. C.; Trans. Faraday Soc. 29 (1933) 1310. Van Risseghem, H.; Bull. Soc. Chim. Belg. 42 (1933) 219. Vosburgh, W. C.; Connell, L. C.; Butler, J. A. V.; J. Chem. Soc. (1933) 933. Whitmore, F. C.; Evers, W. L.; J. Am. Chem. Soc. 55 (1933) 812. Whitmore, F. C.; Herndon, J. M.; J. Am. Chem. Soc. 55 (1933) 3428. Whitmore, F. C.; Homeyer, A. H.; J. Am. Chem. Soc. 55 (1933) 4194. Whitmore, F. C.; Homeyer, A. H.; J. Am. Chem. Soc. 55 (1933) 4555. Whitmore, F. C.; Krueger, P. A.; J. Am. Chem. Soc. 55 (1933) 1528. Whitmore, F. C.; Laughlin, K. C.; J. Am. Chem. Soc. 55 (1933) 3732. Whitmore, F. C.; Williams, F. E.; J. Am. Chem. Soc. 55 (1933) 406. Whitmore, F. C.; Woodburn, H. M.; J. Am. Chem. Soc. 55 (1933) 361. Burdick, H. E.; Adkins, H.; J. Am. Chem. Soc. 56 (1934) 438. Carter, E. G.; Jones, D. C.; Trans. Faraday Soc. 30 (1934) 1027. Cornish, R. E.; Archibald, R. C.; Murphy, E. A.; Evans, H. M.; Ind. Eng. Chem. 26 (1934) 397. Green, J. H.; J. Am. Chem. Soc. 56 (1934) 1167. Jacquemain, R.; Compt. rend. 199 (1934) 1315.

372 34-jac-6 34-lal 34-les/lom 34-pau 34-smi 34-sta 34-tim/del 34-von/man 34-was/spe 35-bil/gis 35-bra/fel 35-bru/fur 35-but/ram 35-but/ram-1 35-col 35-col-1 35-cou/hop 35-cox/rei 35-gib 35-gre-2 35-gui 35-has/mcb 35-hen 35-kef/mcl 35-les/lom 35-lev/har 35-lev/mar 35-mah-1 35-ols/was 35-pau-2 35-sav 35-saw 35-sch/sta 35-tim/hen 36-dup-1 36-ern/wat 36-ipa/cor 36-lev/rot-1 36-naz 36-nor/has 36-oli 36-pal/sab 36-par 36-pow/bal 36-rom 36-spe 36-sto/rou 36-tom 36-tuo 36-wie 37-alb 37-bra

References Jacquemain, R.; Compt. rend. 198 (1934) 482. Lalande, A.; Bull. Soc. Chim. Fr. 1 (1934) 236. Lespieau, R.; Lombard, R.; C. R. Hebd. Seances Acad. Sci. 198 (1934) 2179. Paul, R.; Bull. Soc. Chim. Fr. 1 (1934) 971. Smith, D. M.; Ind. Eng. Chem. 26 (1934) 392. Stahly, E. E.; PhD Dissertation, Pennsylvania State Univeristy (1934) . Timmermans, J.; Delcourt, Y.; J. Chim. Phys. Phys.-Chim. Biol. 31 (1934) 85. Von Braun, J.; Manz, G.; Chem. Ber. 67 (1934) 1696. Washburn, E. R.; Spencer, H. C.; J. Am. Chem. Soc. 56 (1934) 361. Bilterys, R.; Gisseleire, J.; Bull. Soc. Chim. Belg. 44 (1935) 567. Bratton, A. C.; Felsing, W. A.; Bailey, J. R.; Ind. Eng. Chem. 28 (1935) 424. Brunjes, A. S.; Furnas, C. C.; Ind. Eng. Chem. 27 (1935) 396. Butler, J. A. V.; Ramchandani, C. N.; Thomson, D. W.; J. Chem. Soc. (1935) 280. Butler, J. A. V.; Ramchandani, C. N.; J. Chem. Soc. (1935) 952. Colonge, J.; Bull. Soc. Chim. Fr. 2 (1935) 57. Colonge, J.; Bull. Soc. Chim. Fr. 2 (1935) 754. Coull, J.; Hope, H. B.; J. Phys. Chem. 39 (1935) 967. Cox, W. M.; Reid, E. E.; J. Am. Chem. Soc. 57 (1935) 1801. Gibson, R. E.; J. Am. Chem. Soc. 57 (1935) 1551. Gredy, B. ; Bull. Soc. Chim. Fr. 2 (1935) 1038. Guillemonat, A.; C. R. Hebd. Seances Acad. Sci. 200 (1935) 1416. Hass, H. B.; McBee, E. T.; Weber, P.; Ind. Eng. Chem. 27 (1935) 1190. Hennings, C.; Z. Phys. Chem., Abt. B 28 (1935) 267. Keffler, L.; MacLean, J. H.; J. Soc. Chem. Ind., London, Trans. Commun. 54 (1935) 178. Lespieau, R.; Lombard, R.; Bull. Soc. Chim. Fr. 2 (1935) 369. Levene, P. A.; Harris, S. A.; J. Biol. Chem. 112 (1935) 195. Levene, P. A.; Marker, R. E.; J. Biol. Chem. 110 (1935) 299. Mahanti, P. C.; Z. Phys. 94 (1935) 220. Olsen, A. L.; Washburn, E. R.; J. Am. Chem. Soc. 57 (1935) 303. Paul, R.; Bull. Soc. Chim. Fr. 2 (1935) 311. Savard, J.; Bull. Soc. Chim. Fr. 2 (1935) 633. Sawai, I.; Trans. Faraday Soc. 31 (1935) 765. Schierholtz, O. J.; Staples, M. L.; J. Am. Chem. Soc. 57 (1935) 2709. Timmermans, J.; Hennaut-Roland, M.; J. Chim. Phys. Phys.-Chim. Biol. 32 (1935) 501 Dupire, A.; C. R. Hebd. Seances Acad. Sci. 202 (1936) 2086. Ernst, R. C.; Watkins, C. H.; Ruwe, H. H.; J. Phys. Chem. 40 (1936) 627. Ipatieff, V. N.; Corson, B. B.; Pines, H.; J. Am. Chem. Soc. 58 (1936) 919. Levene, P. A.; Rothen, A.; Meyer, G. M.; Kuna, M.; J. Biol. Chem. 115 (1936) 401. Nazarov, I. N.; Chem. Ber. 69 (1936) 21. Norton, F. H.; Hass, H. B.; J. Am. Chem. Soc. 58 (1936) 2147. Olivier, S. C. J.; Recl. Trav. Chim. Pays-Bas 55 (1936) 1027. Palfray, L.; Sabetay, S.; Bull. Soc. Chim. Fr. 3 (1936) 682. Parthasarathy, P. S.; Proc. Indian Acad. Sci., Sect. A 4 (1936) 59. Powell, S. G.; Baldwin, M. M.; J. Am. Chem. Soc. 58 (1936) 1871. Romstatt, G.; Ind. Chim. (Paris) 23 (1936) 567. Spells, K. E.; Trans. Faraday Soc. 32 (1936) 530. Stoll, M.; Rouve, A.; Helv. Chim. Acta 19 (1936) 253. Tomonari, T.; Z. Phys. Chem., Abt. B 32 (1936) 202. Tout, M.; C. R. Hebd. Seances Acad. Sci. 202 (1936) 1339. Wiemann, J.; Ann. Chim. (Paris) 5 (1936) 267. Albright, P. S.; J. Am. Chem. Soc. 59 (1937) 2098. Brauns, D. H.; J. Res. Natl. Bur. Stand. (U. S.) 18 (1937) 315.

Landolt-Börnstein New Series IV/8G

References 37-bra/kur 37-dob/gut 37-dol/bri 37-ewe 37-gib/kin 37-gin/bau 37-mas 37-mil/sus 37-mou/dod 37-naz 37-oli 37-pat/hol 37-pet/and 37-pet/mal 37-puk 37-she/mat 37-tis 37-tis/chu 37-tya 37-zep 38-bak/smy 38-dol/gre 38-gin/hau 38-gin/web 38-hil/adk 38-hov/lan 38-mas 38-ols/was 38-sca/ray 38-tur 38-wer/bog 38-whi/joh 38-whi/kar 38-whi/mey 38-whi/ole 38-whi/ole-1 38-whi/ore 38-whi/pop 38-whi/pop-1 39-all/lin 39-bar/atk 39-cop/gos 39-dup/dar 39-gin/col 39-gol/tay 39-hus/gui 39-jon/chr 39-ken/pla

Landolt-Börnstein New Series IV/8G

373

Braun, J. V.; Kurtz, P.; Chem. Ber. 70 (1937) 1224. Dobrjanski, A. F.; Gutner, R. A.; Shchigel'skaya, M. K.; Zh. Obshch. Khim. 7 (1937) 132. Dolian, F. E.; Briscoe, H. T.; J. Phys. Chem. 41 (1937) 1129. Ewert, M.; Bull. Soc. Chim. Belg. 46 (1937) 90. Gibson, R. E.; Kincaid, J. F.; J. Am. Chem. Soc. 59 (1937) 579. Ginnings, P. M.; Baum, R.; J. Am. Chem. Soc. 59 (1937) 1111. Mastagli, P.; C. R. Hebd. Seances Acad. Sci. 204 (1937) 1656. Milas, N. A.; Sussman, S.; J. Am. Chem. Soc. 59 (1937) 2345. Moureu, H.; Dode, M.; Bull. Soc. Chim. Fr. 4 (1937) 637. Nazarov, I. N.; Chem. Ber. 70 (1937) 599. Olivier, S. C. J.; Recl. Trav. Chim. Pays-Bas 56 (1937) 247. Patterson, T. S.; Holmes, G. M.; J. Chem. Soc. (1937) 1007. Petrov, A. D.; Andreev, D. N.; J. Gen. Chem. USSR (Engl. Transl.) 7 (1937) 570. Petrov, A. D.; Malinovskii, M. S.; J. Gen. Chem. USSR (Engl. Transl.) 7 (1937) 565. Pukirev, A. B.; Tr. Inst. Chist. Khim. Reakt. 15 (1937) 45. Sherrill, M. L.; Matlack, L. S.; J. Am. Chem. Soc. 59 (1937) 2134. Tishchenko, D. V.; Zh. Obshch. Khim. 7 (1937) 658. Tishchenko, D. V.; Churbakov, A. N.; Zh. Obshch. Khim. 7 (1937) 893. Tyazhelova, A. A.; Tr. Voronezh. Gos. Univ. 9(3) (1937) 139. Zepalova-Mikhailova, L. A.; Tr. Inst. Chist. Khim. Reakt. No. 15 (1937) 3. Baker, W. O.; Smyth, C. P.; J. Am. Chem. Soc. 60 (1938) 1229. Dolliver, M. A.; Gresham, T. L.; Kistiakowsky, G. B.; Smith, E. A.; Vaughan, W. E.; J.; Am. Chem. Soc. 60 (1938) 440. Ginnings, P. M.; Hauser, M.; J. Am. Chem. Soc. 60 (1938) 2581. Ginnings, P. M.; Webb, R.; J. Am. Chem. Soc. 60 (1938) 1388. Hill, R. M.; Adkins, H.; J. Am. Chem. Soc. 60 (1938) 1033. Hovorka, F.; Lankelma, H. P.; Stanford, S. C.; J. Am. Chem. Soc. 60 (1938) 820. Mastagli, P.; Ann. Chim. (Paris) 10 (1938) 281. Olsen, A. L.; Washburn, E. R.; J. Phys. Chem. 42 (1938) 275. Scatchard, G.; Raymond, C. L.; J. Am. Chem. Soc. 60 (1938) 1278. Turpeinen, O.; J. Am. Chem. Soc. 60 (1938) 56. Werner, J.; Bogert, M. T.; J. Org. Chem. 3 (1938) 578. Whitmore, F. C.; Johnston, F.; J. Am. Chem. Soc. 60 (1938) 2265. Whitmore, F. C.; Karnatz, F. A.; J. Am. Chem. Soc. 60 (1938) 2533. Whitmore, F. C.; Meyer, R. E.; Pedlow, G. W.; Popkin, A. H.; J. Am. Chem. Soc. 60 (1938) 2788. Whitmore, F. C.; Olewine, J. H.; J. Am. Chem. Soc. 60 (1938) 2569. Whitmore, F. C.; Olewine, J. H.; J. Am. Chem. Soc. 60 (1938) 2570. Whitmore, F. C.; Orem, H. P.; J. Am. Chem. Soc. 60 (1938) 2573. Whitmore, F. C.; Popkin, A. H.; Whitaker, J. S.; Mattil, K. F.; Zech, J. D.; J. Am. Chem. Soc. 60 (1938) 2458. Whitmore, F. C.; Popkin, A. H.; Whitaker, J. S.; Mattil, K. F.; Zech, J. D.; J. Am. Chem. Soc. 60 (1938) 2462. Allen, B. B.; Lingo, S. P.; Felsing, W. A.; J. Phys. Chem. 43 (1939) 425. Barrow, F.; Atkinson, R. G.; J. Chem. Soc. (1939) 638. Coppock, J. B. M.; Goss, F. R.; J. Chem. Soc. (1939) 1789. Dupont, G.; Darmon, M.; Bull. Soc. Chim. Fr. 6 (1939) 1208. Ginnings, P. M.; Coltrane, D.; J. Am. Chem. Soc. 61 (1939) 525. Goldwasser, S.; Taylor, H. S.; J. Am. Chem. Soc. 61 (1939) 1751. Huston, R. C.; Guile, R. L.; J. Am. Chem. Soc. 61 (1939) 69. Jones, G.; Christian, S. M.; J. Am. Chem. Soc. 61 (1939) 82. Kenyon, J.; Platt, B. C.; J. Chem. Soc. (1939) 633.

374 39-lar/hun 39-mar/wil 39-owe/qua 39-par/moo 39-pet/sum 39-spi/tin-1 39-ste/mcn 39 stu/adk 40-gos-1 40-hov/lan 40-hov/lan-1 40-hov/lan-2 40-mil/bli 40-mon/qui 40-mos 40-pal 40-sut 40-tri/ric 40-was/beg 40-was/gra 40-whi/sur 41-boh 41-cam/eby-1 41-dor/gla 41-fav/oni 41-gib/loe 41-gle 41-hea/tam 41-hov/lan 41-hus/age 41-hus/gui 41-whe 41-whi/mos 41-whi/whi

41-whi/wil 42-air/bal 42-boe/han 42-boe/han-1 42-boh 42-bri/rin 42-hen/all 42-moe 42-mul 42-pet/che 42-pum/hah 42-sch/hun

References Larson, R. G.; Hunt, H. ; J. Phys. Chem. 43 (1939) 417. Marvel, C. S.; Williams, W. W.; J. Am. Chem. Soc. 61 (1939) 2714. Owen, K.; Quayle, O. R.; Beavers, E. M.; J. Am. Chem. Soc. 61 (1939) 900. Parks, G. S.; Moore, G. E.; J. Chem. Phys. 7 (1939) 1066. Petrov, A. D.; Sumin, I. G.; Meerovich, Z. A.; Kudrina, K. N.; Tikhonova, G. N.; Zh. Obshch. Khim. 9 (1939) 2144. Spiegler, L.; Tinker, J. M.; J. Am. Chem. Soc. 61 (1939) 940. Stevens, P. G.; McNiven, N. L.; J. Am. Chem. Soc. 61 (1939) 1295 Stutsman, P. S.; Adkins, H.; J. Am. Chem. Soc. 61 (1939) 3303 Goss, F. R.; J. Chem. Soc. (1940) 883. Hovorka, F.; Lankelma, H. P.; Schneider, I.; J. Am. Chem. Soc. 62 (1940) 1096. Hovorka, F.; Lankelma, H. P.; Axelrod, A. E.; J. Am. Chem. Soc. 62 (1940) 187. Hovorka, F.; Lankelma, H. P.; Smith, W. R.; J. Am. Chem. Soc. 62 (1940) 2372. Miller, H. C.; Bliss, H.; Ind. Eng. Chem. 32 (1940) 123. Mondain-Monval, P.; Quiquerez, J.; Bull. Soc. Chim. Fr. 7 (1940) 240. Mosher, W. A.; Ph.D. Dissertation, Penn. State Univ., Univ. Park, PA (1940) . Palfray, L.; Bull. Soc. Chim. Fr. 7 (1940) 401. Sutherland, L. H.; Ph.D. Thesis, Penn. State Univ., Univ. Park, PA, (1940) . Trimble, H. M.; Richardson, E. L.; J. Am. Chem. Soc. 62 (1940) 1018. Washburn, E. R.; Beguin, A. E.; J. Am. Chem. Soc. 62 (1940) 579. Washburn, E. R.; Graham, C. L.; Arnold, G. B.; Transue, L. F.; J. Am. Chem. Soc. 62 (1940) 1454. Whitmore, F. C.; Surmatis, J. D.; J. Am. Chem. Soc. 62 (1940) 995. Bohnsack, H.; Chem. Ber. 74 (1941) 1575. Campbell, K. N.; Eby, L. T.; J. Am. Chem. Soc. 63 (1941) 2683. Dorough, G. L.; Glass, H. B.; Gresham, T. L.; Malone, G. B.; Reid, E. E.; J. Am. Chem. Soc. 63 (1941) 3100. Favorskii, A. E.; Onishchenko, A. S.; Zh. Obshch. Khim. 11 (1941) 1111. Gibson, R. E.; Loeffler, O. H.; J. Am. Chem. Soc. 63 (1941) 898. Gleim, C. E.; Ph.D. Thesis, Penn. State Univ., Univ. Park, PA (1941) . Hearne. G.; Tamele, M.; Converse, W.; Ind. Eng. Chem. 33 (1941) 805. Hovorka, F.; Lankelma, H. P.; Bishop, J. W.; J. Am. Chem. Soc. 63 (1941) 1097. Huston, R. C.; Agett, A. H.; J. Org. Chem. 6 (1941) 123. Huston, R. C.; Guile, R. L.; Sculati, J. J.; Wasson, W. N.; J. Org. Chem. 6 (1941) 252. Wheeler, W. R.; Thesis, Penn. State University, (1941) . Whitmore, F. C.; Mosher, W. A.; J. Am. Chem. Soc. 63 (1941) 1120. Whitmore, F. C.; Whitaker, J. S.; Mosher, W. A.; Breivik, O. N.; Wheeler, W. R.; Miner, C. S.; Sutherland, L. H.; Wagner, R. B.; Clapper, T. W.; Lewis, C. E.; Lux, A. R.; Popkin, A. H.; J. Am. Chem. Soc. 63 (1941) 643. Whitmore, F. C.; Wilson, C. D.; Capinjola, J. V.; Tongberg, C. O.; Fleming, G. H.; McGrew, R. V.; Cosby, J. N.; J. Am. Chem. Soc. 63 (1941) 2035. Airs, R. S.; Balfe, M. P.; Kenyon, J.; J. Chem. Soc. (1942) 18. Boeseken, J.; Hanegraaff, J. A.; Recl. Trav. Chim. Pays-Bas 61 (1942) 69. Boeke, J.; Hanewald, K. H.; Recl. Trav. Chim. Pays-Bas 61 (1942) 881. Bohnsack, H.; Chem. Ber. 75 (1942) 502. Briscoe, H. T.; Rinehart, W. T.; J. Phys. Chem. 46 (1942) 387. Henze, H. R.; Allen, B. B.; Leslie, W. B.; J. Org. Chem. 7 (1942) 326. Moersch, G. W.; Ph.D. Thesis, Penn. State Univ., Univ. Park, PA, (1942). Muller, A.; Fette Seifen 49 (1942) 572. Petrov, A. D.; Chel'tsova, M. A.; J. Gen. Chem. USSR (Engl. Transl.) 12 (1942) 87. Pummerer, R.; Hahn, H.; Johne, F.; Kehlen, H.; Ber. Dtsch. Chem. Ges. 75 (1942) 867 Schumacher, J. E.; Hunt, H. ; Ind. Eng. Chem. 34 (1942) 701.

Landolt-Börnstein New Series IV/8G

References 42-sny/gil 42-was/bro 42-whi/for 43-boh 43-bra 43-bru/bog 43-col/jol 43-dur/roe 43-geo 43-gre/kel 43-hsu 43-ish/kat 43-jam 43-kul/nor 43-lan/key 43-ste/gre 44-app/dob 44-gla 44-hen/mat 44-hus/awu 44-ira 44-mor/aue 44-pow/hag 44-pre 44-pre/zal 44-qua/sma 44-sto/rou 44-was/str 44-you/rob 45-add 45-alb/was 45-dul 45-hen/gre 45-kol/bur 45-len/dup 45-sch 45-sch/gel 46-bra 46-cle-1 46-dou-1 46-fri/sto 46-haf/lov 46-hus/bai 46-kno/sch 46-kre/now 46-lau/wie 46-par/row 46-par/wes 46-pre/val 46-puc/wis

Landolt-Börnstein New Series IV/8G

375

Snyder, H. B.; Gilbert, E. C.; Ind. Eng. Chem. 34 (1942) 1519. Washburn, E. R.; Brockway, C. E.; Graham, C. L.; Deming, P.; J. Am. Chem. Soc. 64 (1942) 1886. Whitmore, F. C.; Forster, W. S.; J. Am. Chem. Soc. 64 (1942) 2966. Bohnsack, H.; Chem. Ber. 76 (1943) 564. Brauns, D. H.; J. Res. Natl. Bur. Stand. (U. S.) 31 (1943) 83. Brunjes, A. S.; Bogart, M. J. P.; Ind. Eng. Chem. 35 (1943) 255. Colonge, J.; Joly, D.; Ann. Chim. (Paris) 18 (1943) 286. Durodie, J.; Roelens, E.; Bull. Soc. Chim. Fr. 10 (1943) 169. George, R. S.; Ph.D. Thesis, Penn. State Univ., Univ. Park, PA (1943) . Green, M. W.; Kelly, K. L.; Steinmetz, C. A.; Bull. Nat. Formul. Comm. 11 (1943) 91. Hsu, P. T.; Ann. Chim. (Paris) 18 (1943) 185. Ishiguro, T.; Kato, S.; Akazawa, Y.; Yakugaku Zasshi 63 (1943) 282. James, W. H.; Ph.D. Thesis, Penn. State Univ., Univ. Park, PA, (1943) . Kulpinski, M. S.; Nord, F. F.; J. Org. Chem. 8 (1943) 256. Langdon, W. M.; Keyes, D. B.; Ind. Eng. Chem. 35 (1943) 459. Stevens, P. G.; Greenwood, S. H. J.; J. Am. Chem. Soc. 65 (1943) 2153. Appleby, W. G.; Dobratz, C. J.; Kapranos, S. W.; J. Am. Chem. Soc. 66 (1944) 1938. Glacet, C.; C. R. Hebd. Seances Acad. Sci. 218 (1944) 283. Henne, A. L.; Matuszak, A. H.; J. Am. Chem. Soc. 66 (1944) 1649. Huston, R. C.; Awuapara, J.; J. Org. Chem. 9 (1944) 401. Irany, E. P.; J. Am. Chem. Soc. 65 (1944) 1392. Morell, S. A.; Auernheimer, A. H.; J. Am. Chem. Soc. 66 (1944) 792. Powell, S. G.; Hagemann, F.; J. Am. Chem. Soc. 66 (1944) 372. Prevost, C.; Bull. Soc. Chim. Fr. 11 (1944) 218. Prelog, V.; Zalan, E.; Helv. Chim. Acta 27 (1944) 545. Quayle, O. R.; Smart, K. O.; J. Am. Chem. Soc. 66 (1944) 935. Stoll, M.; Rouve, A.; Helv. Chim. Acta 27 (1944) 950. Washburn, E. R.; Strandskov, C. V.; J. Phys. Chem. 48 (1944) 241. Young, W. G.; Roberts, J. D.; J. Am. Chem. Soc. 66 (1944) 1444. Addison, C. C.; J. Chem. Soc. (1945) 98. Alberty, R. A.; Washburn, E. R.; J. Phys. Chem. 49 (1945) 4. Dulitskaya, K. A.; Zh. Obshch. Khim. 15 (1945) 9. Henne, A. L.; Greenlee, K. W.; J. Am. Chem. Soc. 67 (1945) 484. Kolb, H. J.; Burwell, R. L.; J. Am. Chem. Soc. 67 (1945) 1084. Lenth, C. W.; Dupuis, R. N.; Ind. Eng. Chem. 37 (1945) 152. Schmerling, L.; J. Am. Chem. Soc. 67 (1945) 1152. Schniepp, L. E.; Geller, H. H.; J. Am. Chem. Soc. 67 (1945) 54 Brauns, H.; Recl. Trav. Chim. Pays-Bas 65 (1946) 799. Clendenning, K. A.; Can. J. Res., Sect. B 24 (1946) 269. Doumani, T.; Patent, U.S. 2,394,848, Feb. 12, (1946) . Fritzsche, R. H.; Stockton, D. L.; Ind. Eng. Chem. 38 (1946) 737. Hafslund, E. R.; Lovell, C. L.; Ind. Eng. Chem. 38 (1946) 556. Huston, R. C.; Bailey, D. L.; J. Am. Chem. Soc. 68 (1946) 1382. Knowlton, J. W.; Schieltz, N. C.; Macmillan, D.; J. Am. Chem. Soc. 68 (1946) 208. Kretschmer, C. B.; Nowakowska, J.; Wiebe, R.; Ind. Eng. Chem. 38 (1946) 506. Laude, G.; Wiemann, J.; Bull. Soc. Chim. Fr. (1946) 256. Parks, G. S.; Rowe, R. D.; J. Chem. Phys. 14 (1946) 507. Parks, G. S.; West, T. J.; Naylor, B. F.; Fujii, P. S.; McClaine, L. A.; J. Am. Chem. Soc. 68 (1946) 2524. Prevost, C.; Valette, A.; C. R. Hebd. Seances Acad. Sci. 222 (1946) 326. Puck, T. T.; Wise, H.; J. Phys. Chem. 50 (1946) 329.

376 46-shi 46-sim/was 46-vav/col 47-col/lag 47-det/cra 47-dev 47-how/mea 47-kor/lic 47-rei/dem 47-sch/sch 47-sho/pri 47-sto 47-str/gab 47-tuo/guy 48-adk/bil 48-bae/fis 48-bou/nic 48-bro/bro 48-cad/foo 48-con/elv 48-goe/cri 48-hus/goe 48-hus/kra 48-jon/bow 48-kor/pat 48-kre/now 48-lad/smi 48-laz 48-mal/kon 48-mcm/rop 48-mic/hop 48-naz/tor 48-pet/old 48-pow/nie 48-pro/cas 48-pud 48-rit 48-ruo 48-sor/sor 48-val 48-vog-2 48-wei 48-zal 48-zas 49-ber/ped

References Shikheev, I. A.; Zh. Obshch. Khim. 16 (1946) 657. Simonsen, D. R.; Washburn, E. R.; J. Am. Chem. Soc. 68 (1946) 235. Vavon, G.; Colin, H.; C. R. Hebd. Seances Acad. Sci. 222 (1946) 801. Colonge, J.; Lagier, A.; C. R. Hebd. Seances Acad. Sci. 224 (1947) 572. Detling, K. D.; Crawford, C. C.; Yabroff, D. L.; Peterson, W. H.; Patent, Brit. 591,632, Aug. 25, (1947) . De Vrieze, J. J.; Recl. Trav. Chim. Pays-Bas 66 (1947) 486. Howard, F. L.; Mears, T. W.; Fookson, A.; Pomerantz, P.; Brooks, D. B.; J. Res. Natl. Bur. Stand. (U. S.) 38 (1947) 365. Kornblum, N.; Lichtin, N. N.; Patton, J. T.; Iffland, D. C.; J. Am. Chem. Soc. 69 (1947) 307. Reinders, W.; De Minjer, C. H.; Recl. Trav. Chim. Pays-Bas 66 (1947) 552. Schinz, H.; Schappi, G.; Helv. Chim. Acta 30 (1947) 1483. Shostakovskii, M. F.; Prilezhaeva, E. N.; Zh. Obshch. Khim. 17 (1947) 1129. Stoll, M.; Helv. Chim. Acta 30 (1947) 991. Stross, F. H.; Gable, C. M.; Rounds. G. C.; J. Am. Chem. Soc. 69 (1947) 1629. Tuot, M.; Guyard, M.; Bull. Soc. Chim. Fr. (1947) 1086. Adkins, H.; Billica, H. R.; J. Am. Chem. Soc. 70 (1948) 3121. Baer, E. B.; Fischer, H. O. L.; J. Am. Chem. Soc. 70 (1948) 609. Bourns, A. N.; Nicholls, R. V. V.; Can. J. Res., Sect. B 26 (1948) 81. Brokaw, G. Y.; Brode, W. R.; J. Org. Chem. 13 (1948) 194. Cadwallader, E. A.; Fookson, A.; Mears, T. W.; Howard, F. L.; J. Res. Natl. Bur. Stand. (U. S.) 41 (1948) 111. Conner, A. Z.; Elving, P. J.; Steingiser, S.; Ind. Eng. Chem. 40 (1948) 497. Goering, H. L.; Cristol, S. J.; Dittmer, K.; J. Am. Chem. Soc. 70 (1948) 3314. Huston, R. C.; Goerner, G. L.; Breining, E. R.; Bostwick, C. O.; Cline, K. D.; Snyder, L. J.; J. Am. Chem. Soc. 70 (1948) 1090. Huston, R. C.; Krantz, R. J.; J. Org. Chem. 13 (1948) 63. Jones, W. J.; Bowden, S. T.; Yarnold, W. W.; Jones, W. H.; J. Phys. Colloid Chem. 52 (1948) 753. Kornblum, N.; Patton, J. T.; Nordmann, J. B.; J. Am. Chem. Soc. 70 (1948) 746. Kretschmer, C. B.; Nowakowska, J.; Wiebe, R.; J. Am. Chem. Soc. 70 (1948) 1785. Laddha, G. S.; Smith, J. M.; Ind. Eng. Chem. 40 (1948) 494. Lazzari, G.; Ann. Chim. Appl. 38 (1948) 287. Malinovskii, M. S.; Konevichev, E. N.; Zh. Obshch. Khim. 18 (1948) 1833. Mcmahon, E. M.; Roper, J. N.; Utermohlen, W. P.; Hasek, R. H.; Harris, R. C.; Brant, J. H.; J. Am. Chem. Soc. 70 (1948) 2971. Michael, T. H. G.; Hopkins, C. Y.; Can. Chem. Process Ind. 32 (1948) 341. Nazarov, I. N.; Torgov, I. V.; Zh. Obshch. Khim. 18 (1948) 1480. Petrov, A. D.; Ol'dekop, Y. A.; Zh. Obshch. Khim. 18 (1948) 859. Powell, S.; Nielsen, A.; J. Am. Chem. Soc. 70 (1948) 3627. Prout, F. S.; Cason, J.; Ingersoll, A. W.; J. Am. Chem. Soc. 70 (1948) 298. Pudovik, A. N.; Zh. Obshch. Khim. 19 (1948) 1187. Ritter, J. J.; J. Am. Chem. Soc. 70 (1948) 4253. Ruof, C. H.; Ph.D. Thesis, Penn. State Univ., Univ. Park, PA, (1948) Sorensen, J. S.; Sorensen, N. A.; Acta Chem. Scand. 2 (1948) 166. Valette, P. A.; Ann. Chim. (Paris) 3 (1948) 644. Vogel, A. I.; J. Chem. Soc. (1948) 1814. Weissler, A.; J. Am. Chem. Soc. 70 (1948) 1634. Zal'manovich, M. Z.; Zh. Obshch. Khim. 18 (1948) 2103. Zaslavskii, I. I.; Zh. Prikl. Khim. (Leningrad) 21 (1948) 732. Bernstein, H. J.; Pedersen, E. E.; J. Chem. Phys. 17 (1949) 885.

Landolt-Börnstein New Series IV/8G

References 49-boo/gre 49-bru 49-col/lag 49-dre/mar 49-gri/chu 49-hat 49-hat-1 49-hat-2 49-hos/ste 49-ken/str 49-kre/wie-1 49-mal/vol 49-moe/whi 49-naz/pin 49-naz/zar-1 49-pra/dra 49-tsc/ric 49-tsv/mar 49-udo/kal 49-vve/iva 50-ada/van 50-boe/ned 50-cle/mac 50-cro/van 50-doe/zei 50-fav/fri 50-gor 50-hou/mas-1 50-jac 50-lad/smi 50-let/tra 50-mea/foo 50-mos/lac 50-mum/phi 50-naz/bak 50-naz/fis 50-naz/kot-1 50-par/gol 50-pau/tch 50-pic/zie 50-sac/sau 50-ste/coo 50-tei/gor 50-vie 50-wol/sau 51-ami/wei 51-ber-2 51-bot

Landolt-Börnstein New Series IV/8G

377

Boord, C. E.; Greenlee, K. W.; Perilstein, W. L.; Derfer, J. M.; Am. Pet. Inst. Res. Proj. 45, Eleventh Annu. Rep., Ohio State Univ., June (1949) . Bruner, W. M.; Ind. Eng. Chem. 41 (1949) 2860. Colonge, J.; Lagier, A.; Bull. Soc. Chim. Fr. (1949) 15. Dreisbach, R. R.; Martin, R. A.; Ind. Eng. Chem. 41 (1949) 2875. Griswold, J.; Chu, P. L.; Winsauer, W. O.; Ind. Eng. Chem. 41 (1949) 2352. Hatem, S.; Bull. Soc. Chim. Fr. (1949) 337. Hatem, S.; Bull. Soc. Chim. Fr. (1949) 483. Hatem, S.; Bull. Soc. Chim. Fr. (1949) 599. Hosman, B. B. A.; Van Steenis, J.; Waterman, H. I.; Recl. Trav. Chim. Pays-Bas 68 (1949) 939. Kenyon, J.; Strauss, H. E.; J. Chem. Soc. (1949) 2153. Kretschmer, C. B.; Wiebe, R.; J. Am. Chem. Soc. 71 (1949) 3176. Malinovskii, M. S.; Volkova, E. E.; Morozova, N. M.; Zh. Obshch. Khim. 19 (1949) 114. Moersch, G. W.; Whitmore, F. C.; J. Am. Chem. Soc. 71 (1949) 819. Nazarov, I. N.; Pinkina, L. N.; Zh. Obshch. Khim. 19 (1949) 1870. Nazarov, I. N.; Zaretskaya, I. I.; Izv. Akad. Nauk SSSR Ser. Khim. (1949) 184. Pratt, E. F.; Draper, J. D.; J. Am. Chem. Soc. 71 (1949) 2846. Tschamler, H.; Richter, E.; Wettig, F.; Monatsh. Chem. 80 (1949) 749. Tsvetkov, V. N.; Marinin, V. A.; Dokl. Akad. Nauk SSSR 68 (1949) 49 Udovenko, V. V.; Kalabanovskaya, E. I.; Prokop'eva, M. F.; Zh. Obshch. Khim. 19 (1949) 165. Vvedenskii, A. A.; Ivannikov, P. Ya.; Nekrasova, V. A.; Zh. Obshch. Khim. 19 (1949) 1094 Adams, R. M.; Vanderwerf, C. A.; J. Am. Chem. Soc. 72 (1950) 4368. Boelhouwer, J. W. M.; Nederbragt, G. W.; Verberg, G. W.; Appl. Sci. Res., Sect. A 2 (1950) 249. Clendenning, K. A.; Macdonald, F. J.; Wright, D. E.; Can. J. Res., Sect. B 28 (1950) 608. Croxall, W. J.; Van Hook, J. O.; J. Am. Chem. Soc. 72 (1950) 803. Doering, W. von E.; Zeiss, H. H.; J. Am. Chem. Soc. 72 (1950) 147. Favorskaya, T. A.; Fridman, Sh. A.; Zh. Obshch.Khim. 20 (1950) 413. Gorin, Y.; Zh. Obshch. Khim. 20 (1950) 1596. Hough, E. W.; Mason, D. M.; Sage, B. H.; J. Am. Chem. Soc. 72 (1950) 5775. Jacobson, B.; Ark. Kemi 2 (1950) 177. Laddha, G. S.; Smith, J. M.; Chem. Eng. Prog. 46 (1950) 195. Letsinger, R. L.; Traynham, J. G.; J. Am. Chem. Soc. 72 (1950) 849. Mears, T. W.; Fookson, A.; Pomerantz, P.; Rich, E. H.; Dussinger, C. S.; Howard, F. L.; J. Res. Natl. Bur. Stand. (U. S.) 44 (1950) 299. Mosher, H. S.; La Combe, E.; J. Am. Chem. Soc. 72 (1950) 3994. Mumford, S. A.; Phillips, J. W. C.; J. Chem. Soc. (1950) 75. Nazarov, I. N.; Bakhmutskaya, S. S.; Zh. Obshch. Khim. 20 (1950) 1837. Nazarov, I. N.; Fisher, L. B.; Zh. Obshch. Khim. 20 (1950) 1107. Nazarov, I. N.; Kotlyarevskii, P. A.; Zh. Obshch. Khim. 20 (1950) 1449. Parker, E. D.; Goldblatt, L. A.; J. Am. Chem. Soc. 72 (1950) 2151. Paul, R.; Tchelitcheff, S.; Bull. Soc. Chim. Fr. (1950) 520. Pichler, H.; Ziesecke, K. H.; Traeger, B.; Brennst.-Chem. 31 (1950) 361. Sackmann, H.; Sauerwald, F.; Z. Phys. Chem. (Leipzig) 195 (1950) 295. Stehman, C. J.; Cook, N. C.; Percival, W. C.; Whitmore, F. C.; J. Am. Chem. Soc. 72 (1950) 4163. Teitel'baum, B. Ya.; Gortalova, T. A.; Ganelina, S. G.; Zh. Obshch. Khim. 20 (1950) 1422. Vierk, A.-L ; Z. Anorg. Chem. 261 (1950) 283. Wolf, F.; Sauerwald, F.; Kolloid-Z. 118 (1950) 1. Amick, E. H.; Weiss, M. A. ; Kirshenbaum, M. S.; Ind. Eng. Chem. 43 (1951) 969. Bergmann, E. D.; Patent, U.S. 2,539,806, Jan. 30, (1951) . Bothner-By, A. A.; J. Am. Chem. Soc. 73 (1951) 846.

378 51-cop/fie 51-dim/lan 51-dra-1 51-dub 51-gor 51-hau 51-hub 51-kre 51-ler/luc 51-lev/fai 51-lyu/ter 51-mac/tho 51-mca/cul 51-sew 51-smi/cre 51-sor/suc 51-tei/gor 51-van-1 51-wat/coo 51-whi/dea 52-cap/mug 52-coo 52-cur/joh 52-doe/far 52-dun/was 52-eri-1 52-gri 52-hel 52-her/zao 52-hug/mal 52-ino 52-kip/tes 52 lev/shu 52-lev/tan 52-mye/col 52-ove/ber 52-pet/she 52-pom 52-roe/stu 52-sta/spi 52-van 52-von 52-wib 52-wil/sch 52-wil/sim 53-ame/pax 53-ani 53-ani-1

References Copet, A.; Fierens-Snoeck, M. P.; Van Risseghem, H.; Bull. Soc. Chim. Fr. (1951) 902. Dimmling, W.; Lange, E.; Z. Elektrochem. 55 (1951) 322. Drahowzal, F.; Monatsh. Chem. 82 (1951) 794. Dubois, J. E. ; Ann. Chim. (Paris) 6 (1951) 406. Gorge, M.; Ann. Chim. (Paris) 6 (1951) 649. Hausermann, M.; Helv. Chim. Acta 34 (1951) 1211. Huber, W. F.; J. Am. Chem. Soc. 73 (1951) 2730. Kretschmer, C. B.; J. Phys. Colloid Chem. 55 (1951) 1351. Leroux, P. J.; Lucas, H. J. ; J. Am. Chem. Soc. 73 (1951) 41. Levina, R. Ya.; Fainzil'berg, A. A.; Tantsyreva, T. I.; Treshchova, E. G.; Izv. Akad. Nauk SSSR Ser. Khim. (1951) 321. Lyubomilov, V. I.; Terent'ev, A. P.; Zh. Obshch. Khim. 21 (1951) 1479. Macbeth, G.; Thompson, A. R.; Anal. Chem. 23 (1951) 618. McAllan, D. T.; Cullum, T. V.; Dean, R. A.; Fidler, F. A.; J. Am. Chem. Soc. 73 (1951) 3627. Seward, R. P.; J. Am. Chem. Soc. 73 (1951) 515. Smith, F. A.; Creitz, E. C.; J. Res. Natl. Bur. Stand. (U. S.) 46 (1951) 145. Sorm, F.; Suchy, M.; Herout, V.; Chem. Listy 45 (1951) 218. Teitel'baum, B. Ya.; Gortalova, T. A.; Sidorova, E. E.; Zh. Fiz. Khim. 25 (1951) 911. Van Risseghem, H.; Bull. Soc. Chim. Fr. 18 (1951) 908. Watson, R. W.; Coope, J. A. R.; Barnwell, J. L.; Can. J. Chem. 29 (1951) 885. Whitehead, E. V.; Dean, R. A.; Fidler, F. A.; J. Am. Chem. Soc. 73 (1951) 3632. Capitani, C.; Mugnaini, E.; Chim. Ind. (Milan) 34 (1952) 193. Cook, N. C.; Unpublished, Final Rep. Stand. Proj. on Oxygenated Compounds, Penn. State Univ., College Park, PA, (1952) . Curme, G. O.; Johnston, F.; Glycols, Reinhold Publishing Corp., New York (1952) . Doering, W. von E.; Farber, M.; Sprecher, M.; Wiberg, K. B.; J. Am. Chem. Soc. 74 (1952) 3000. Dunning, H. N.; Washburn, E. W.; J. Phys. Chem. 56 (1952) 235. Erichsen, L.; Brennst.-Chem. 33 (1952) 166. Griffiths, V. S.; J. Chem. Soc. (1952) 1326. Heller, H. E.; J. Am. Chem. Soc. 74 (1952) 4858. Herout, V.; Zaoral, M.; Sorm, F.; Chem. Listy 46 (1952) 156. Hughes, H. E.; Maloney, J. O.; Chem. Eng. Prog. 48 (1952) 192. Inoue, H.; Yakugaku Zasshi 72 (1952) 731. Kipling, J. J.; Tester, D. A.; J. Chem. Soc. (1952) 4123. Levina, R. Ya.; Shusherina, N. P.; Treshchova, E. G.; Vestn. Mosk. Univ., Ser. Fiz.-Mat. Estestv. Nauk 7 (1952) 105 Levina, R. Ya.; Tantsyreva, T. I.; Fainzil'berg, A. A.; Zh. Obshch. Khim. 22 (1952) 571. Myers, R. T.; Collett, A. R.; Lazzell, C. L.; J. Phys. Chem. 56 (1952) 461. Overberger, C. G.; Berenbaum, M. B.; J. Am. Chem. Soc. 74 (1952) 3293. Petrov, A. D.; Shebanova, M. P.; Dokl. Akad. Nauk SSSR 84 (1952) 721. Pomerantz, P.; J. Res. Natl. Bur. Stand. (U. S.) 48 (1952) 76. Roe, E. T.; Stutzman, J. M.; Scanlan, J. T.; Swern, D.; J. Am. Oil Chem. Soc. 29 (1952) 18. Staveley, L. A. K.; Spice, B.; J. Chem. Soc. (1952) 406. Van Risseghem, H.; Bull. Soc. Chim. Fr. (1952) 177. Von Erichsen, L.; Brennst.-Chem. 33 (1952) 166. Wiberg, K. B.; J. Am. Chem. Soc. 74 (1952) 3891. Willimann, L.; Schinz, H.; Helv. Chim. Acta 35 (1952) 2401. Wilson, A.; Simons, E. L.; Ind. Eng. Chem. 44 (1952) 2214. Amer, H. H.; Paxton, R. R.; Van Winkle, M.; Anal. Chem. 25 (1953) 1204. Anisimov, V. I.; Zh. Fiz. Khim. 27 (1953) 1797. Anisimov, V. I.; Zh. Fiz. Khim. 27 (1953) 674.

Landolt-Börnstein New Series IV/8G

References 53-ano-1 53-ano-5 53-ano-6 53-ano-15 53-bar-5 53-bar/bro 53-cha/mou 53-col/dre 53-dan/fad 53-gru/ost 53-hag/dec 53-hat/jou 53-her/zao 53-ish/kat 53-kha/kud 53-kre-1 53-mcc/jon 53-mck/tar 53-ner/hen 53-ots/wil 53-par/cha 53-per/wag 53-pin/hun 53-raz/old 53-sok 53-sut 54-ano-12 54-bre 54-dub/luf 54-fre/lwo 54-gay/cro 54-gri 54-jon/mcc 54-kre/wie 54-mcc/pro 54-mos/cox 54-naz/kak-1 54-naz/kak-2 54-naz/kak-3 54-naz/kak-4 54-pom/foo 54-pom/foo-1 54-pur/bow 54-rin/ari 54-ros 54-ser/voi-1 54-ski/flo 54-skr/mur

Landolt-Börnstein New Series IV/8G

379

Am. Pet. Inst. Res. Proj. 45, Fifteenth Annu. Rep., Ohio State Univ., June (1953) . Am. Pet. Inst. Res. Proj. 6, Carnegie-Mellon Univ., May (1953) . Coal Tar Data Book, 1st ed., Coal Tar Research Assoc.: Gomersal, Leeds, (1953) . Union Carbide & Carbon Corporation, unpublished (1953) . Barkan, A. S.; Proc. Byelorussian State Univ. Issue 14 (1953) 108. Barker, J. A.; Brown, I.; Smith, F.; Discuss. Faraday Soc. No. 15 (1953) 142. Chang, Y.; Moulton, R. W.; Ind. Eng. Chem. 45 (1953) 2350. Colonge, J.; Dreux, J.; C. R. Hebd. Seances Acad. Sci. 236 (1953) 1791. Danusso, F.; Fadigati, E.; Atti Accad. Naz. Lincei, Cl. Sci. Fis., Mat. Nat., Rend. 9 (1953) 81. Grubb, W. T.; Osthoff, R. C.; J. Am. Chem. Soc. 75 (1953) 2230. Hagemeyer, H. J.; DeCroes, G. C.; The Chemistry of Isobutylaldehyde and Its Derivatives, Eastman Co.: Tenn., (1953) . Hatch, L. F.; Journeay, G. E. ; J. Am. Chem. Soc. 75 (1953) 3712. Herout, V.; Zaoral, M.; Sorm, F.; Collect. Czech. Chem. Commun. 18 (1953) 122. Ishiguro, T.; Kato, S.; Sakata, Y.; Akazawa, Y.; Yakugaku Zasshi 73 (1953) 1167. Kharasch, M. S.; Kuderna, J.; Nudenberg, W.; J. Org. Chem. 18 (1953) 1225. Kremmling, G.; Z. Naturforsch., A: Astrophys., Phys., Phys. Chem. 8 (1953) 708. McCants, J. F.; Jones, J. H.; Hopson, W. H.; Ind. Eng. Chem. 45 (1953) 454. McKenna, F. E.; Tartar, H. V.; Lingafelter, E. C.; J. Am. Chem. Soc. 75 (1953) 604. Nerdel, F.; Henkel, E.; Chem. Ber. 86 (1953) 1002. Otsuki, H.; Williams, F. C.; Chem. Eng. Prog., Symp. Ser. 49 (1953) 55. Parthasarathy, P. S.; Chari, S. S.; Srinivasan, D.; J. Phys. Radium 14 (1953) 541. Percival, W. C.; Wagner, R. B.; Cook, N. C.; J. Am. Chem. Soc. 75 (1953) 3731. Pines, H.; Huntsman, W. D. ; Ipatieff, V. N.; J. Am. Chem. Soc. 75 (1953) 2311. Razuvaev, G. A.; Ol'dekop, Yu. A.; Zh. Obshch. Khim. 23 (1953) 1173. Sokolova, E. B.; Zh. Obshch. Khim. 23 (1953) 2002. Sutherland, M. D.; J. Am. Chem. Soc. 75 (1953) 5944 Laboratory Data Sheets, Union Carbide Corp, South Charleston WV (1954) . Brey, W. S.; Anal. Chem. 26 (1954) 838. Dubois, J. E. ; Luft, R. ; Bull. Soc. Chim. Fr. (1954) 1148. Freudenberg, K.; Lwowski, W.; Justus Liebigs Ann. Chem. 587 (1954) 213. Gaylord, N. G.; Crowdle, J. H.; Himmler, W. A.; Pepe, H. J.; J. Am. Chem. Soc. 76 (1954) 59. Griffiths, V. S.; J. Chem. Soc. (1954) 860. Jones, J. H.; McCants, J. F.; Ind. Eng. Chem. 46 (1954) 1956. Kretschmer, C. B.; Wiebe, R.; J. Am. Chem. Soc. 76 (1954) 2579. McCasland, G. E.; Proskow, S.; J. Am. Chem. Soc. 76 (1954) 3486. Mosher, W. A.; Cox, J. C.; Grant-in-Aid Application to A.P.I., Univ. of Delaware, April 28, (1954) . Nazarov, I. N.; Kakhniashvili, A. I.; Sb. Statei Obshch. Khim. 2 (1954) 896. Nazarov, I. N.; Kakhniashvili, A. I.; Ryabchenko, V. F.; Sb. Statei Obshch. Khim. 2 (1954) 913. Nazarov, I. N.; Kakhniashvili, A. I.; Sb. Statei Obshch. Khim. 2 (1954) 919. Nazarov, I. N.; Kakhniashvili, A. I.; Sb. Statei Obshch. Khim. 2 (1954) 905. Pomerantz, P.; Fookson, A.; Mears, T. W.; Rothberg, S.; Howard, F. L.; J. Res. Natl. Bur. Stand. (U. S.) 52 (1954) 51. Pomerantz, P.; Fookson, A.; Mears, T. W.; Rothberg, S.; Howard, F. L.; J. Res. Natl. Bur. Stand. (U. S.) 52 (1954) 59 Purnell, J. H.; Bowden, S. T.; J. Chem. Soc. (1954) 539. Riniker, B.; Arigoni, D.; Jeger, O.; Helv. Chim. Acta 37 (1954) 546. Ross, H. K.; Ind. Eng. Chem. 46 (1954) 601. Serpinskii, V. V.; Voitkevich, S. A.; Lyuboshich, N. Yu.; Zh. Fiz. Khim. 28 (1954) 1969. Skinner, G. S.; Florentine, F. P.; J. Am. Chem. Soc. 76 (1954) 3200. Skrzec, A. E.; Murphy, N. F.; Ind. Eng. Chem. 46 (1954) 2245.

380 54-smi/otv 54-tha/row 54-vor/tit 54-wes/aud 55-ano 55-ano-2 55-bak 55-ber/sch 55-blo/ver-1 55-blo/whe 55-bou/cle 55-che/che 55-dan/col 55-fle/sau 55-fog/hix 55-gay/cau 55-ham/sto 55-kay/don 55-kus 55-mes/pet 55-mos 55-nol/pan 55-pet 55-pet/sus 55-sar/mor 55-ser 55-sin/she 55-soe/fre 55-tim/hen 55-wes 56-ame/pax 56-ano-1 56-ano-3 56-ano-4 56-cri 56-fai/win 56-far/she 56-gla/gau 56-goe/mcc 56-gol/kon 56-ike/kep 56-kat/new 56-koi/han 56-kru/cho 56-lev/sch 56-lib/lap-1 56-lic/dur 56-nav/des 56-pri/osg

References Smith, V. N.; Otvos, J. W.; Anal. Chem. 26 (1954) 359. Thacker, R.; Rowlinson, J. S.; Trans. Faraday Soc. 50 (1954) 1036. Voronkov, M. G.; Titlinova, E. S.; Zh. Obshch. Khim. 24 (1954) 613. Westwater, J. W.; Audrieth, L. F.; Ind. Eng. Chem. 46 (1954) 1281. Am. Pet. Inst. Res. Proj. 45, Tech. Rep. 14, No. 1, Ohio State Univ., (1955) . Am. Pet. Inst. Res. Proj. 6, Carnegie-Mellon Univ., Aug. (1955). Baker, E. M.; J. Phys. Chem. 59 (1955) 1182. Beringer, F. M.; Schultz, H. S.; J. Am. Chem. Soc. 77 (1955) 5533. Blomquist, A. T.; Verdol, J. A.; J. Am. Chem. Soc. 77 (1955) 78. Blomquist, A. T.; Wheeler, E. S.; Chu, Y.; J. Am. Chem. Soc. 77 (1955) 6307. Boud, A. H.; Cleverdon, D.; Collins, G. B.; Smith, J. O.; J. Chem. Soc. (1955) 3793. Chel'tsova, M. A.; Chernyshev, E. A.; Petrov, A. D.; Izv. Akad. Nauk SSSR Ser. Khim. (1955) 522. Dannhauser, W.; Cole, R. H.; J. Chem. Phys. 23 (1955) 1762. Fleming, R.; Saunders, L.; J. Chem. Soc. (1955) 4147. Fogg, E. T. ; Hixson, A. N.; Thompson, A. R.; Anal. Chem. 27 (1955) 1609. Gaylord, N. G.; Caul, L. D.; J. Am. Chem. Soc. 77 (1955) 3132. Hammond, B. R.; Stokes, R. H.; Trans. Faraday Soc. 51 (1955) 1641. Kay, W. B.; Donham, W. E.; Chem. Eng. Sci. 4 (1955) 1. Kuss, E.; Z. Angew. Phys. 7 (1955) 372. Meshcheryakov, A. P.; Petrova, L. V.; Izv. Akad. Nauk SSSR Ser. Khim. (1955) 1057. Moshkin, P. A.; Vpr. Isolz. Pentozansoderzh. Syrya Tr. Vses. Soveshch. Riga (1955) 225 Noller, C. R.; Pannell, C. E.; J. Am. Chem. Soc. 77 (1955) 1862. Petrov, A. D.; Izv. Akad. Nauk SSSR Ser. Khim. (1955) 639. Petrov, A. D.; Sushchinskii, V. L.; Konoval'chikov, L. D.; Zh. Obshch. Khim. 25 (1955) 1566. Sarycheva, I. K.; Morozova, N. G.; Abramovich, V. A.; Breitburt, S. A.; Sergienko, L. F.; Preobrazhenskii, N. A.; Zh. Obshch. Khim. 25 (1955) 2001. Serck-Hanssen, K.; Ark. Kemi 8 (1955) 401. Singh, R.; Shemilt, L. W.; J. Chem. Phys. 23 (1955) 1370. Soehring, K.; Frey, H. H.; Endres, G.; Arzneim.-Forsch. 5 (1955) 161. Timmermans, J.; Hennaut-Roland, M.; J. Chim. Phys. Phys.-Chim. Biol. 52 (1955) 223. Westwater, J. H.; Ind. Eng. Chem. 47 (1955) 451. Amer, H. H.; Paxton, R. R.; Van Winkle, M.; Ind. Eng. Chem. 48 (1956) 142. Br. Stand. Vol. 555, Brit. Standards Inst., London (1956) . Physical Properties: Synthetic Organic Chemicals, Carbide and Carbon Chemical Company, (1956) . Am. Pet. Inst. Res. Proj. 6, Carnegie-Mellon Univ., April (1956) . Crisan, C.; Ann. Chim. (Paris) 1 (1956) 436. Fainberg, A. H.; Winstein, S.; J. Am. Chem. Soc. 78 (1956) 2770. Farberov, M. I.; Shemyakina, N. K.; Zh. Obshch. Khim. 26 (1956) 2749. Glacet, C.; Gaumenton, A.; Bull. Soc. Chim. Fr. (1956) 1425. Goering, H. L.; McCarron, F. H.; J. Am. Chem. Soc. 78 (1956) 2270. Gol'dfarb, Ya. L.; Konstantinov, P. A.; Izv. Akad. Nauk SSSR Ser. Khim. (1956) 992. Ikeda, R. M.; Kepner, R. E.; Webb, A. D.; Anal. Chem. 28 (1956) 1335. Katz, K.; Newman, M.; Ind. Eng. Chem. 48 (1956) 137. Koizumi, N.; Hanai, T.; J. Phys. Chem. 60 (1956) 1496. Krug, R. C.; Choate, W. L.; Walbert, J. T.; Leedy, R. C.; J. Am. Chem. Soc. 78 (1956) 1698. Levina, R. Ya.; Schabarov, Yu. S.; Vestn. Mosk. Univ., Ser. 2 Khim. 11 (1956) 61. Liberman, A. L.; Lapshina, T. V.; Kazanskii, B. A.; Zh. Obshch. Khim. 26 (1956) 46 Lichtenberger, J.; Durr, L.; Bull. Soc. Chim. Fr. (1956) 664. Naves, Y. -R.; Desalbres, L.; Ardizio, P.; Bull. Soc. Chim. Fr. (1956) 1713. Price, C. C.; Osgan, M.; J. Am. Chem. Soc. 78 (1956) 4787.

Landolt-Börnstein New Series IV/8G

References 56-rat/cur 56-rus/ame 56-sar/new 56-shu/bel 56-smi/ebe 56-sok/fed 56-tar/tai 56-tor-1 56-woo/vio 57-ano 57-ano-1 57-ano-11 57-bol/ego 57-bol/ego-1 57-chi/tho 57-col/fal 57-cru/jos 57-far/rot 57-fav/ser 57-for/lan 57-gol/kon 57-hic/ken 57-ket/van 57-kit 57-luk/lan 57-mal/mal 57-mur/las 57-naz/kra 57-pet/nef-1 57-pet/sok 57-pet/sus 57-rao/rao 57-rom 57-rom-1 57-sar/vor 57-shu/bel 57-tak/nak 57-tra/bat 58-ano-3 58-ano-5 58-ano-13 58-arn/was 58-col/fal 58-cos/bow 58-ego 58-far/spe 58-hag/hud 58-hen/wat

Landolt-Börnstein New Series IV/8G

381

Rathmann, G. B.; Curtis, A. J.; McGeer, P. L.; Smyth, C. P.; J. Am. Chem. Soc. 78 (1956) 2035. Rush, R. I.; Ames, D. C.; Horst, R. W.; Mackay, J. R.; J. Phys. Chem. 60 (1956) 1591. Sarel, S.; Newman, M. S.; J. Am. Chem. Soc. 78 (1956) 5416. Shuikin, N. I.; Bel'skii, I. F.; J. Gen. Chem. USSR (Engl. Transl.) 26 (1956) 3025. Smith, W. M.; Eberly, K. C.; Hanson, E. E.; Binder, J. L.; J. Am. Chem. Soc. 78 (1956) 626. Sokolova, E. B.; Fedotov, N. S.; Tr. Inst. - Mosk. Khim. -Tekhnol. Inst. im. D. I. Mendeleeva No. 23 (1956) 31. Tarasova, G. A.; Taits, G. S.; Plate, A. F.; Izv. Akad. Nauk SSSR Ser. Khim. (1956)1267. Toropov, A. P.; Zh. Obshch. Khim. 26 (1956) 1453. Woods, G. F.; Viola, A.; J. Am. Chem. Soc. 78 (1956) 4380. Patent, Brit. 776,073, Esso Res. Eng. Co., June 5, (1957) . Patent, Ger. 1,007,772, Farbenfabriken Bayer Akt.-Ges., May 9, (1957) . Laboratory Data Sheets, Union Carbide Corp, South Charleston, WV, (1957) . Bol'shukhin, A. I.; Egorov, A. G.; Zh. Obshch. Khim. 27 (1957) 647. Bol'shukhin, A. I.; Egorov, A. G.; Zh. Obshch. Khim. 27 (1957) 933. Chiao, T. T.; Thomson, A. R.; Anal. Chem. 29 (1957) 1678. Colonge, J.; Falcotet, R.; Bull. Soc. Chim. Fr. (1957) 1166. Cruetzen, J. L.; Jost, W.; Sieg, L.; Z. Elektrochem. 61 (1957) 230. Farberov, M. I.; Rotshtein, Y. I.; Kut'in, A. M.; Shemyakina, N. K.; Zh. Obshch. Khim. 27 (1957) 2806. Favorskaya, T. I.; Sergievskaya, O. V.; Ryzhova, N. P.; Zh. Obshch. Khim. 27 (1957) 937. Foreman, R. W.; Lankelma, H. P.; J. Am. Chem. Soc. 79 (1957) 409. Gol'dfarb, Ya. L.; Konstantinov, P. A.; Izv. Akad. Nauk SSSR Ser. Khim. (1957) 217. Hickman, J. R.; Kenyon, J.; J. Chem. Soc. (1957) 4677. Ketelaar, J. A. A.; Van Meurs, N.; Recl. Trav. Chim. Pays-Bas 76 (1957) 437. Kitoaka, R.; Nippon Kagaku Zasshi 78 (1957) 1594. Lukes, R.; Langthaler, J.; Chem. Listy 51 (1957) 1869. Malyusov, V. A.; Malafeev, N. A.; Zhavoronkov, N. M.; Zh. Fiz. Khim. 31 (1957) 699. Murphy, N. F.; Lastovica, J. E.; Fallis, J. G.; Ind. Eng. Chem. 49 (1957) 1035. Nazarov, I. N.; Krasnaya, Zh. A.; Makin, S. M.; Dokl. Akad. Nauk SSSR 114 (1957) 553. Petrov, A. D.; Nefedov, O. M.; Grigor'ev, F. I.; Zh. Obshch. Khim. 27 (1957) 1876. Petrov, A. D.; Sokolova, E. B.; Kao, C. L.; Izv. Akad. Nauk SSSR Ser. Khim. (1957) 871. Petrov, A. D.; Sushchinskii, V. L.; Zakharov, E. P.; Rogozhnikova, T. I.; Zh. Obshch. Khim. 27 (1957) 467. Rao, M. R.; Rao, C. V.; J. Appl. Chem. 7 (1957) 659. Romadane, I.; Zh. Obshch. Khim. 27 (1957) 1833. Romadane, I.; Zh. Obshch. Khim. 27 (1957) 1939. Sarycheva, I. K.; Vorob'eva, G. A.; Kucheryavenko, L. G.; Preobrazhenskii, N. A.; Zh. Obshch. Khim. 27 (1957) 2994. Shuikin, N. I.; Bel'skii, I. F.; Zh. Obshch. Khim. 27 (1957) 402. Takemoto, T.; Nakajima, T.; Yakugaku Zasshi 77 (1957) 1307. Traynham, J. G.; Battiste, M. A.; J. Org. Chem. 22 (1957) 1551 Patent, Brit. 804,057, Monsanto Chemical Co., Nov. 5, (1958) . Alcohols, Union Carbide Corp., (1958) . Laboratory Data Sheets, Union Carbide Corp, South Charlston, WV, (1958) . Arnold, V. W.; Washburn, E. R.; J. Phys. Chem. 62 (1958) 1088. Colonge, J.; Falcotet, R.; Gaumont, R.; Bull. Soc. Chim. Fr. (1958) 211. Costello, J. M.; Bowden, S. T.; Recl. Trav. Chim. Pays-Bas 77 (1958) 36. Egorov, A. G.; Uch. Zap., Leningr. Gos. Pedagog. Inst. im. A. I. Gertsena 179 (1958) 211. Farberov, M. I.; Speranskaya, V. A.; Zh. Obshch. Khim. 28 (1958) 2151. Hagemeyer, H. J.; Hudson, G. V.; Patent, U.S. 2,852,563, Sept. 16, (1958) . Hennion, G.; Watson, E.; J. Org. Chem. 23 (1958) 656.

382 58-hil/hay 58-hol/len 58-kut/lyu 58-leb/kuk 58-leg/ulr 58-lin/tua 58-lin/van 58-lyu 58-lyu/bel 58-muk/gru 58-mur/van 58-naz/gus 58-oga/tak 58-pan/osi 58-per/can 58-rao/ram 58-sok/kra 58-wag/web 58-wie/thu 58-yam/kun 59-ale 59-ano-7 59-asi/gei 59-bar/dod 59-bur/can 59-col/gau 59-ell/raz 59-fol/wel 59-her 59-hos/nis 59-hou/lev 59-kom/ros 59-lis/kor 59-mac/bar 59-mck/ski 59-nie/web 59-nog/dza 59-pet/zak 59-pet/zak-1 59-pin/lar 59-tsu/hay 59-yur/bel 59-yur/bel-1 60-ano-13 60-cop/fin 60-fro/shr 60-kor/pet 60-kun/sak 60-naz/mak

References Hill, C. M.; Haynes, L.; Simmons, D. E.; Hill, M. E.; J. Am. Chem. Soc. 80 (1958) 3623. Hollo, J.; Lengyel, T.; Uzonyi, G.; Magy. Kem. Lapja 13 (1958) 440. Kutsenko, A. I.; Lyubomilov, V. I.; Zh. Prikl. Khim. (Leningrad) 31 (1958) 1419. Lebedeva, A. I.; Kukhareva, L. V.; Zh. Obshch. Khim. 28 (1958) 2782. LeGoff, E.; Ulrich, S. E.; Denney, D. B.; J. Am. Chem. Soc. 80 (1958) 622. Lin, W.-C.; Tuan, F.-T.; J. Chin. Chem. Soc. (Taipei) 5 (1958) 33. Ling, T. D.; Van Winkle, M.; Chem. Eng. Data Ser. 3 (1958) 88. Lyubomilov, V. I.; Zh. Obshch. Khim. 28 (1958) 328. Lyubomilov, V. I.; Belyanina, E. T.; Zh. Obshch. Khim. 28 (1958) 326. Mukherjee, L. M.; Grunwald, E.; J. Phys. Chem. 62 (1958) 1311. Murti, P. S.; Van Winkle, M.; Chem. Eng. Data Ser. 3 (1958) 72. Nazarov, I. N.; Gussev, B. P.; Gunar, V. I.; Zh. Obshch. Khim. 28 (1958) 1444. Ogata, Y.; Takagi, Y.; J. Am. Chem. Soc. 80 (1958) 3591. Pansevich-Kolyada, V. I.; Osipenko, I. F.; Zh. Obshch. Khim. 28 (1958) 641. Perry, M. A.; Canter, F. C.; DeBusk, R. E.; Robinson, A. G.; J. Am. Chem. Soc. 80 (1958) 3618. Rao, M. R.; Ramamurty, M.; Rao, C. V.; Chem. Eng. Sci. 8 (1958) 265. Sokolova, E. B.; Krasnova, G. V.; Zhurleva, T. A.; Nauchn. Dokl. Vyssh. Shk. Khim. Khim. Tekhnol. (1958) 330. Wagner, I. F.; Weber, J. H.; Chem. Eng. Data 3 (1958) 220. Wiemann, J.; Thuan, L. T.; Bull. Soc. Chim. Fr. (1958) 199. Yamamoto, T.; Kunimoto, S.; Yuki Gosei Kagaku Kyokaishi 16 (1958) 258. Alexander, D. M.; J. Chem. Eng. Data 4 (1959) 252. Laboratory Data Sheets, Union Carbide Corp, South Charleston WV (1959) . Asinger, F.; Geiseler, G.; Schmiedel, K.; Chem. Ber. 92 (1959) 3085. Barr-David, F.; Dodge, B. F.; J. Chem. Eng. Data 4 (1959) 107. Bures, E.; Cano, C.; de Wirth, A.; J. Chem. Eng. Data 4 (1959) 199. Colonge, J.; Gaumont, R.; Bull. Soc. Chim. Fr. (1959) 939. Ellis, S. R. M.; Razavipour, M.; Chem. Eng. Sci. 11 (1959) 99. Foley, W. M.; Welch, F. J.; La Combe, E.; Mosher, H. S.; J. Am. Chem. Soc. 81 (1959) 2779. Herbertz, T.; Chem. Ber. 92 (1959) 541. Hoshiai, K.; Nishio, A.; Patent, Jpn. 2211-2, April 9, (1959) . Houlihan, W. J.; Levy, J.; Mayer, J.; J. Am. Chem. Soc. 81 (1959) 4692. Komandin, A. V.; Rosolovskii, V. Ya.; Zh. Fiz. Khim. 33 (1959) 1280. Lishanskii, I. S.; Korotkov, A. A.; Andreev, G. A.; Zak, A. G.; Zh. Prikl. Khim. (Leningrad) 32 (1959) 2344. Machinskaya, I. V.; Barkhash, V. A.; Zh. Obshch. Khim. 29 (1959) 2786. McKinney, W. P.; Skinner, G. F.; Staveley, L. A. K.; J. Chem. Soc. (1959) 2415. Nielsen, R. L.; Weber, J. H.; J. Chem. Eng. Data 4 (1959) 145. Nogaideli, A. I.; Dzagnidze, K. Ya.; Tr. Tbilis. Univ. 74 (1959) 159. Petrov, A. D.; Zakharov, E. P.; Izv. Vyssh. Uchebn. Zaved., Khim. Khim. Tekhnol. 2 (1959) 384. Petrov, A. D.; Zakharov, E. P.; Krasnova, T. L.; Zh. Obshch. Khim. 29 (1959) 49. Pino, P.; Lardicci, L.; Centoni, L.; J. Org. Chem. 24 (1959) 1399. Tsuda, K. ; Hayatsu, R.; Kishida, Y.; Chem. Ind. (London) (1959) 1411. Yur'ev, Yu. K.; Belyakova, Z. V.; Zh. Obshch. Khim. 29 (1959) 2960. Yur'ev, Yu. K.; Belyakova, Z. V.; Volkov, V. P.; Zh. Obshch. Khim. 29 (1959) 3652 Laboratory Data Sheets, Union Carbide Corp, South Charleston WV (1960) . Copp, J. L.; Findlay, T. J. V.; Trans. Faraday Soc. 56 (1960) 13. Frontas'ev, V. P.; Shraiber, L. S.; Uch. Zap. Sarat. Gos. Univ. 69 (1960) 225. Kormer, V. A.; Petrov, A. A.; Zh. Obshch. Khim. 30 (1960) 3890. Kunitika, S.; Sakakibara, Y.; Nippon Kagaku Zasshi 81 (1960) 140. Nazarov, I. N.; Makin, S. M.; Nazarova, D. V.; Mochalin, V. B.; Shavrygina, O. A.; Zh. Obshch. Khim. 30 (1960) 1168.

Landolt-Börnstein New Series IV/8G

References 60-oak/web 60-pet/kao 60-pet/sok 60-por/far 60-rab/mur 60-ter/kep 60-tha/vas 60-tje 60-tsu/kis 61-ano-11 61-bel/shu-1 61-bel/web 61-des/del 61-dyk/sep 61-hat/wei 61-lut/obu 61-mar/pet 61-mes/erz 61-mil/ben 61-ogi/cor 61-sch-3 61-shv/pet 61-sok/she 61-tis/sta 61-wib/fos 61-yeh 62-and/kuk-1 62-ber/leg 62-ber/leg-1 62-ber/mol 62-bog/osi 62-bro/smi 62-chu/tho 62-col/des 62-col/gir 62-cuv/nor 62-deg/lad 62-esa/shi 62-esa/zhu 62-fav/por 62-gei/fru 62-gei/qui 62-kae/web 62-kuh/kuh 62-lar/sal

Landolt-Börnstein New Series IV/8G

383

Oakeson, G. O.; Weber, J. H.; J. Chem. Eng. Data 5 (1960) 279. Petrov, A. D.; Kao, C. L.; Semenkin, V. M.; Zh. Obshch. Khim. 30 (1960) 363. Petrov, A. D.; Sokolova, E. B.; Kao, C. L.; Zh. Obshch. Khim. 30 (1960) 1107. Porsch, F.; Farnow, H.; Dragoco Rep. (Engl. Ed.) 7 (1960) 215. Rabinovich, I. B.; Murzin, V. I.; Zhilkin, L. S.; Russ. J. Phys. Chem. (Engl. Transl.) 34 (1960) 937. Terry, T. D.; Kepner, R. E.; Dinsmore, W.; J. Chem. Eng. Data 5 (1960) 403. Thaker, K. A.; Vasi, I. G.; J. Sci. Ind. Res., Sect. B 19 (1960) 322. Tjebbes, J.; Acta Chem. Scand. 14 (1960) 180. Tsuda, K. ; Kishida, Y.; Hayatsu, R.; J. Am. Chem. Soc. 82 (1960) 3396. Laboratory Data Sheets, Union Carbide Corp, South Charleston WV (1961) . Bel'chev, F. V.; Shuikin, N. I.; Novikov, S. S.; Bull. Acad. Sci. USSR Div. Chem. Sci. (1961) 599. Belknap, R. C.; Weber, J. H.; J. Chem. Eng. Data 6 (1961) 485. Desgrandchamps, G.; Deluzarche, A.; Maillard, A.; Bull. Soc. Chim. Fr. (1961) 264. Dykyj, J.; Seprakova, M.; Paulech, J.; Chem. Zvesti 15 (1961) 465. Hatch, L. F.; Weiss, H. D.; Li, T. P.; J. Org. Chem. 26 (1961) 61. Lutskii, A. E.; Obukhova, E. M.; J. Gen. Chem. USSR (Engl. Transl.) 31 (1961) 2522. Maretina, I. A.; Petrov, A. A.; Zh. Obshch. Khim. 31 (1961) 419. Meshcheryakov, A. P.; Erzyutova, E. I.; Kuo, Chun-I; Izv. Akad. Nauk SSSR Ser. Khim. (1961) 2198. Miller, R. E.; Bennett, G. E.; Ind. Eng. Chem. 53 (1961) 33. Ogimachi, N. N.; Corcoran, J. M.; Kruse. H. W.; J. Chem. Eng. Data 6 (1961) 238. Schwenker, G.; Arch. Pharm. Ber. Dtsch. Pharm. 294 (1961) 661. Shvarts, E. Yu.; Petrov, A. A.; Zh. Obshch. Khim. 31 (1961) 433. Sokolova, E. B.; Shebanova, M. P.; Shchepinov; Izv. Vyssh. Uchebn. Zaved., Khim. Khim. Tekhnol. 4 (1961) 617. Tishchenko, I. G.; Stanishevskii, L. S.; Zhidkofazn. Okislenie Nepredel'nykh Org. Soedin. No. 1 (1961) 133. Wiberg, K. B.; Foster, G.; J. Am. Chem. Soc. 83 (1961) 423. Yeh, P. H.; Riechst. Aromen 11 (1961) 285. Andreevskii, D. N.; Kukharskaya, E. V.; Zh. Obshch. Khim. 32 (1962) 1353. Bertrand, M.; Le Gras, J.; Bull. Soc. Chim. Fr. (1962) 2136. Bertrand, M.; Le Gras, J.; C. R. Hebd. Seances Acad. Sci. 255 (1962) 1305. Bergel'son, L. D.; Molotkovskii, Yu. G.; Shemyakin, M. M.; Zh. Obshch. Khim. 32 (1962) 58. Bogatskaya, Z. D.; Osipchuk, V. P.; Ti, F.-P.; Gol'mov, V. P.; Zh. Obshch. Khim. 32 (1962) 2282. Brown, I.; Smith, F.; Aust. J. Chem. 15 (1962) 3. Chu, K.-Y.; Thompson, A. R.; J. Chem. Eng. Data 7 (1962) 358. Colonge, J.; Descotes, G.; Soula, J. C.; C. R. Hebd. Seances Acad. Sci. 254 (1962) 887. Colonge, J.; Girantet, A.; Bull. Soc. Chim. Fr. (1962) 1002. Cuvigny, T.; Normant, H.; C. R. Hebd. Seances Acad. Sci. 254 (1962) 316. Degaleesan, T. E.; Laddha, G. S.; J. Appl. Chem. 12 (1962) 111. Esafov, V. I.; Shitoz, G. P.; Zh. Obshch. Khim. 32 (1962) 2819. Esafov, V. I.; Zhukova, L. P.; J. Gen. Chem. USSR (Engl. Transl.) 32 (1962) 2775. Favorskaya, T. A.; Portnyagin, Yu. M.; Zh. Obshch. Khim. 32 (1962) 2122. Geiseler, G.; Fruwert, J.; Stockel, E.; Z. Phys. Chem. (Munich) 32 (1962) 330. Geiseler, G.; Quitzsch, K.; Hesselbach, J.; Huettig, R.; Z. Phys. Chem. (Leipzig) 220 (1962) 79. Kaes, G. L.; Weber, J. H.; J. Chem. Eng. Data 7 (1962) 344. Kuhn, R.; Kum, K.; Chem. Ber. 95 (1962) 2009. Lardicci, L.; Salvadori, R.; Pino, P.; Ann. Chim. (Rome) 52 (1962) 652.

384 62-mau/smi 62-mel 62-mir/fed 62-nik/vor 62-par/mis 62-par/mos 62-pet/kap 62-raz/bog 62-ste/van 62-thi 62-yur/pen 62-yur/rev 63-aga/men 63-amb/tow 63-brz/har 63-col/bue 63-esa 63-gol/bag 63-hov/sea 63-kud/sus-1 63-lab 63-lyu/mer 63-man/she 63-man/she-1 63-mcc/lai 63-mik/kim 63-nik 63-pra/van 63-pra/van-1 63-raj/ran 63-shu/bar 63-sub/rao-1 63-tho/mea 63-tho/pal 63-tsy/sol 63-vil/gav 63-yeh 64-ber/lon 64-ber/vav 64-bla/per-1 64-blo/hag 64-bog/kug 64-col/var 64-dan/bah 64-des/sou 64-esa/das

References Maurit, M. E.; Smirnova, G. V.; Parfenov, E. A.; Vinkovskaya, T. M.; Preobrazhenskii, N. A.; Zh. Obshch. Khim. 32 (1962) 2483. Mellan, I.; Polyhydric Alcohols, Spartan Books: Washington, DC, (1962) . Miropol'skaya, M. A.; Fedotova, N. I.; Veinberg, A. Ya.; Yanotovskii, M. T.; Samokhvalov, G. I.; Zh. Obshch. Khim. 32 (1962) 2214. Nikishin, G. I.; Vorobev, V. D.; Izv. Akad. Nauk SSSR Ser. Khim. (1962) 892. Paraskevopoulos, G. C.; Missen, R. W.; Trans. Faraday Soc. 58 (1962) 869. Parks, G. S.; Mosher, H. P.; J. Chem. Phys. 37 (1962) 919. Petrov, A. D.; Kaplan, E. P.; Zh. Obshch. Khim. 32 (1962) 693. Razuvayev, G.; Boguslavskaya, L. S.; Zh. Obshch. Khim. 32 (1962) 2320. Stephenson, R. W.; Van Winkle, M.; J. Chem. Eng. Data 7 (1962) 510. Thi, T. S. L.; C. R. Hebd. Seances Acad. Sci. 254 (1962) 3873. Yur'ev, Yu. K.; Pentin, Y. A.; Revenko, O. M.; Lebedeva, E. I.; Neftekhimiya 2 (1962) 137. Yur'ev, Y.; Revenko, O. M.; Vestn. Mosk. Univ., Ser. 2: Khim. 17 (1962) 68. Agarwal, M. M.; Mene, P. S.; Indian Chem. Eng. 5 (1963) 71. Ambrose, D.; Townsend, R.; J. Chem. Soc. 54 (1963) 3614. Brzostowski, W.; Hardman, T. M.; Bull. Acad. Pol. Sci., Ser. Sci. Chim. 11 (1963) 447. Colonge, J.; Buendia, J.; C. R. Hebd. Seances Acad. Sci. 257 (1963) 2663. Esafov, V. I.; Zh. Obshch. Khim. 33 (1963) 3755. Golubev, I. F.; Bagina, E. N.; Tr. GIAP (1963) 39. Hovermale, R. A.; Sears, P. G.; Plucknett, W. K.; J. Chem. Eng. Data 8 (1963) 490. Kudryavtseva, L. S.; Susarev, M. P.; Zh. Prikl. Khim. (Leningrad) 36 (1963) 1471. Labarre, J. F.; Ann. Chim. 8 (1963) 45. Lyubomilov, V. I.; Merkula, N. N.; Zh. Obshch. Khim. 33 (1963) 22. Mann, R. S.; Shemilt, L. W.; J. Chem. Eng. Data 8 (1963) 189. Mann, R. S.; Shemilt, L. W.; Waldichuck, M.; J. Chem. Eng. Data 8 (1963) 502. McCurdy, K. G.; Laidler, K. J.; Can. J. Chem. 41 (1963) 1867. Mikhail, S. Z.; Kimel, W. R.; J. Chem. Eng. Data 8 (1963) 323. Niklas, H.; Chem. Ber. 96 (1963) 818. Prabhu, P. S.; Van Winkle, M.; J. Chem. Eng. Data 8 (1963) 210. Prabhu, P. S.; Van Winkle, M.; J. Chem. Eng. Data 8 (1963) 14. Raju, B. N.; Ranganathan, R.; Narasinga Rao, M.; Indian Chem. Eng. 5 (1963) 82. Shuikin, N. I.; Bartok, M.; Karakhanov, R. A.; Shostakovskii, V. M.; Acta Phys. Chem. 9 (1963) 124. Subbarao, B. V.; Rao, C. V.; J. Chem. Eng. Data 8 (1963) 368. Thomas, L. H.; Meatyard, R.; J. Chem. Soc. (1963) 1986. Thomas, A. F.; Palluy, E.; Willhalm, B.; Stoll, M.; Helv. Chim. Acta 46 (1963) 2089. Tsyrkel, T. M.; Solov'eva, N. P.; Voltkevich, S. A.; Dushestykh Veshchestv No. 6 (1963) 15. Vil'shau, K. V.; Gavrilova, V. A.; Tr. IREA No. 25 (1963) 347. Yeh, P. H.; Am. Perfum. Cosmet. 78 (1963) 32. Bertocchio, R.; Longeray, R.; Dreux, J.; Bull. Soc. Chim. Fr. (1964) 60. Bergel'son, L. D.; Vaver, V. A.; Bezzubov, A. A.; Shemyakin, M. M.; Izv. Akad. Nauk SSSR Ser. Khim. (1964) 1453. Blanc, P. Y.; Perret, A.; Teppa, F.; Helv. Chim. Acta 47 (1964) 567. Blood, A. E.; Hagemeyer, H. H.; Patent, Fr. 1,359,089, April 24, (1964) . Bogdanova, A. V.; Kugatova, G. P.; Volkov, A. N.; Arakelyan, V. G.; Izv. Akad. Nauk. SSSR Ser. Khim. (1964) 174. Colonge, J.; Varagnat, A.; Bull. Soc. Chim. Fr. (1964) 2499. Dannhauser, W.; Bahe, L. W.; J. Chem. Phys. 40 (1964) 3058. Descotes, G.; Soula, J. C.; Bull. Soc. Chim. Fr. (1964) 2636. Esafov, V. I.; Dashko, V. N.; Narek, E. M.; Zh. Obshch. Khim. 34 (1964) 4094.

Landolt-Börnstein New Series IV/8G

References 64-hel/dav 64-hin/dre 64-mys/zie 64-nog/rtv 64-ohl/sei 64-pol/bel 64-sca/sat 64-ska/kay 64-sta-1 64-sta/kor 64-tis/sta 64-zak/sta 65-alb/bry 65-bar/koz 65-col/des 65-das/mae 65-fav/nik 65-fin/kid 65-mig/mig 65-mor/lam 65-por/pli 65-red/rao 65-rum 65-shu/puz 65-vij/des 65-wei/lan 66-are/tav 66-bue 66-bue-1 66-efr 66-far/per 66-fre/hor 66-gar/kom 66-gur/raj 66-kat/pra-1 66-kat/shi 66-kil/che 66-koz/rab 66-mil-1 66-mya/pya 66-per/bal 66-rob/edm 66-vij/des 66 vla/vas 67-ano-5 67-dav/fin 67-dei 67-fre

Landolt-Börnstein New Series IV/8G

385

Hellin, M.; Davidson, M.; Lumbroso, D.; Giuliani, P.; Coussemant, F.; Bull. Soc. Chim. Fr. (1964) 2974. Hinnen, A.; Dreux, J.; Bull. Soc. Chim. Fr. (1964) 1492. Myszkowski, J.; Zielinski, A. Z.; Mikolajewicz, M.; Przem. Chem. 43 (1964) 383. Nogaideli, A. I.; Rtveliashvilli, N. A.; Zh. Obshch. Khim. 34 (1964) 1737. Ohloff, G.; Seibl, J.; Kovats, E.; Justus Liebigs Ann. Chem. 675 (1964) 83. Polyakova, K. S.; Belov, V. N.; Zh. Obshch. Khim. 34 (1964) 565. Scatchard, G.; Satkiewicz, F. G.; J. Am. Chem. Soc. 86 (1964) 130. Skaates, J. M.; Kay, W. B.; Chem. Eng. Sci. 19 (1964) 431. Stanley, H. M.; Patent, Fr. 1,361,772, May 22, (1964) . Stadnichuk, T. V.; Kormer, V. A.; Petrov, A. A.; Zh. Obshch. Khim. 34 (1964) 3279. Tishchenko, I. G.; Stanishevskii, L. S.; Geterog. Reakts. Reakts. Sposobn. (1964) 254. Zakharkin, L. I.; Stanko, V. I.; Brattsev, V. A.; Izv. Akad. Nauk SSSR Ser. Khim. (1964) 931. Al'bitskaya, V. M.; Bryskovskaya, A. V.; Zh. Org. Khim. 1 (1965) 429. Bartok, M.; Kozma, B.; Gilde, A. S.; Acta Phys. Chem. 11 (1965) 35. Colonge, J.; Descotes, G.; Bahurel, Y.; Bull. Soc. Chim. Fr. (1965) 619. Dashunin, V. M.; Maeva, R. V.; Zh. Org. Khim. 1 (1965) 996. Favorskaya, I. A.; Nikitina, A. A.; Zh. Organ. Khim. 1 (1965) 2094. Findlay, T. J. V.; Kidman, A. D.; Aust. J. Chem. 18 (1965) 521. Miginiac-Groizeleau, L.; Miginiac, P.; Prevost, C.; Bull. Soc. Chim. Fr. (1965) 3560. Mornet, R.; Lamant, M.; Riobe, O.; Bull. Soc. Chim. Fr. (1965) 3043. Pormale, M. Ya.; Plisko, E. A.; Danilov, S. N.; J. Org. Chem. USSR 1 (1965) 1788. Reddy, M. S.; Rao, C. V.; J. Chem. Eng. Data 10 (1965) 309. Rummens, F. H. A.; Recl. Trav. Chim. Pays-Bas 84 (1965) 1003. Shutikova, L. A.; Puzitskii, K. V.; Cherkaev, V. G.; Eidus, Y. T.; Tr. Vses. Nauchno-Issled. Inst. Sint. Nat. Dushistykh Veshchestv. No. 7 (1965) 16. Vijayaraghavan, S. V.; Deshpande, P. K.; Kuloor, N. R.; Indian J. Technol. 3 (1965) 267. Weiss, F.; Lantz, A.; Lakodey, A.; France Patent 1,409,376 (1965) Areshidze, Kh. I.; Tavartkiladze, E. K.; Soobshch. Akad. Nauk Gruz. SSR 41 (1966) 315 Buendia, J.; Bull. Soc. Chim. Fr. (1966) 2781. Buendia, J.; Bull. Soc. Chim. Fr. (1966) 3600. Efremov, Yu. V.; Zh. Fiz. Khim. 40 (1966) 1240. Farina, M.; Peronaci, E. M.; Chim. Ind. (Milan) 48 (1966) 602. Freifeld, M.; Hort, E. V.; Kirk-Othmer Encyc. Chem. Technol., 2nd Ed. 10 (1966) 667. Garber, Yu. N.; Komarova, L. F.; Zh. Prikl. Khim. (Leningrad) 39 (1966) 1366. Gurukul, S. M. K. A.; Raju, B. N.; J. Chem. Eng. Data 11 (1966) 501. Katti, P. K.; Prakash, O.; J. Chem. Eng. Data 11 (1966) 46. Katti, P. K.; Shil, S. K.; J. Chem. Eng. Data 11 (1966) 601. Killgore, C. A.; Chew, W. W.; Orr, V.; J. Chem. Eng. Data 11 (1966) 535. Kozlov, N. A.; Rabenovich, I. B.; Melkii, A. V.; J. Appl. Chem. USSR (Engl. Transl.) 39 (1966) 1290. Miller, P. H.; Kirk-Othmer Encyc. Chem. Technol., 2nd Ed. 10 (1966) 638. Myagkova, G. I.; Pyatnova, Yu. B.; Sarycheva, I. K.; Preobrazhenskii, N. A.; J. Org. Chem. USSR (Engl. Transl.) 2 (1966) 1961. Perepelkin, O. V.; Bal'yan, K. V.; Zh. Org. Khim. 2 (1966) 1928. Robinson, R. L.; Edmister, W. C.; Dullien, F. A. L.; Ind. Eng. Chem. Fundam. 5 (1966) 74. Vijayaraghavan, S. V.; Deshpande, P. K.; Kuloor, N. R.; J. Chem. Eng. Data 11 (1966) 147. Vlasov, V. M.; Vasil'eva, A. A.; Semenova, E. F.; Zh. Org. Khim. 2 (1966) 595. Laboratory Data Sheets, Union Carbide Corp, South Charleston WV (1967) . Davids, E. L.; Findlay, T. J. V.; Aust. J. Chem. 20 (1967) 1343. Deich, A. Y.; Latv. PSR Zinat. Akad. Vestis Kim. Ser. No. 1 (1967) 9. Freshwater, D. C.; J. Chem. Eng. Data 12 (1967) 179.

386 67-gol/per 67-kom/man 67-min/che 67-mis/sub 67-mur/rao 67-nat/rao 67-pis/gas 67-seu/mor 67-sho/ata 67-vij/des-1 67-zal/aru 68-ana/rao 68-ano 68-eva/lin 68-joh 68-kaw/min 68-naz/tsy 68-pfl/pop 68-rao/chi 68-sin/ben 68-ver 69-ada 69-bro/foc 69-fin/cop 69-kat/pat 69-kom/kri 69-nav/tul 69-pat/kat 69-smi/kur 69-sub/nag 69-ver/lau 69-zub/bag 70-are/tav 70-che/tho 70-gal 70-gar/kom 70-gur/raj 70-kat/kon 70-kon/lya 70-kri/kom 70-kri/kom-1 70-kun/cha 70-min/kaw 70-mye/cle 70-nak/shi 70-paz/paz

References Gold, P. I.; Perrine, R. L.; J. Chem. Eng. Data 12 (1967) 4. Komarenko, V. G.; Manzhelii, V. G.; Radtsig, A. V.; Ukr. Fiz. Zh. (Ukr. Ed.) 12 (1967) 676. Min'kovskii, M. M.; Cherkaev, V. G.; Maslozhir. Prom. 33 (1967) 31. Mishchenko, K. P.; Subbotina, V. V.; Zh. Prikl. Khim. (Leningrad) 40 (1967) 1156. Muralimohan, S.; Rao, P. B.; J. Chem. Eng. Data 12 (1967) 494. Nataraj, V.; Rao, M. R.; Indian J. Technol. 5 (1967) 212. Pischnamassade, B. F.; Gasanova, S. D.; Azerb. Khim. Zh. 2 (1967) 60. Seucan, S.; Moraru, E.; Avramescu, E.; Metrol. Apl. 14 (1967) 313. Shostakovskii, M. F.; Atavin, A. S.; Vasil'ev, N. P.; Mikhaleva, A. I.; Dmitrieva, L. P.; J. Org. Chem. USSR (Engl. Transl.) 3 (1967) 2072. Vijayaraghavan, S. V.; Deshpande, P. K.; Kuloor, N. R.; J. Chem. Eng. Data 12 (1967) 13. Zalinyan, M. G.; Arutyunyan, V. S.; Dangyan, M. T.; Arm. Khim. Zh. 20 (1967) 620. Ananthanarayanan, P.; Rao, P. B.; J. Chem. Eng. Data 13 (1968) 194. Chemicals and Plastics Physical Properties, Union Carbide Corp. (product bulletin), (1968) . Evans, L. R.; Lin, J. S.; J. Chem. Eng. Data 13 (1968) 14. Johari, G. P.; J. Chem. Eng. Data 13 (1968) 541. Kawasaki, T.; Minowa, Z.; Inamatsu, T.; Bull. Nat. Res. Lab. Metrol., Tokyo No. 17 (1968) 114. Nazarova, S. S.; Tsyskovskii, V. K.; Ogurtsova, N. A.; Zh. Prikl. Khim. (Leningrad) 41 (1968) 144. Pflug, H. D.; Pope, A. E.; Benson, G. C.; J. Chem. Eng. Data 13 (1968) 408. Rao, P. R.; Chiranjivi, C.; Dasarao, C. J.; J. Appl. Chem. 18 (1968) 166. Singh, J.; Benson, G. C.; Can. J. Chem. 46 (1968) 1249. Verhoeye, L. A. J.; J. Chem. Eng. Data 13 (1968) 462. Adamcova, Z.; Coll. Czech. Chem. Comm. 34 (1969) 3149. Brown, I.; Fock, W.; Smith, F.; J. Chem. Thermodyn. 1 (1969) 273. Findlay, T. J. V.; Copp, J. L.; Trans. Faraday Soc. 65 (1969) 1463. Katti, P. K.; Pathak, C. M.; J. Chem. Eng. Data 14 (1969) 73. Komarov, V. M.; Krichevtsov, B. K.; Zh. Prikl. Khim. (Leningrad) 42 (1969) 2772. Naves, Y. -R.; Tullen, P.; Bull. Soc. Chim. Fr. (1969) 586. Pathak, S.; Katti, S. S.; J. Chem. Eng. Data 14 (1969) 359. Smirnova, N. A.; Kurtynina, L. M.; Zh. Fiz. Khim. 43 (1969) 1883. Subramanian, D.; Nageshwar, G. D.; Mene, P. S.; J. Chem. Eng. Data 14 (1969) 421. Verhoeye, L. A. J.; Lauwers, E.; J. Chem. Eng. Data 14 (1969) 306. Zubarev, V. N.; Bagdonas, A.; Teploenergetika (Moscow) 16 (1969) 88 Areshidze, Kh. I.; Tavartkiladze, E. K.; Chivadze, G. O.; J. Appl. Chem. USSR (Engl. Transl.) 43 (1970) 606. Chen, D. H. T.; Thompson, A. R.; J. Chem. Eng. Data 15 (1970) 471. Galska-Krajewska, A.; Rocz. Chem. 44 (1970) 1255. Garber, Yu. N.; Komarova, L. F.; Aleinikova, L. I.; Fomina, L. S.; Zh. Prikl. Khim. (Leningrad) 43 (1970) 2658. Gurukul, S. M. K. A.; Raju, B. N.; J. Chem. Eng. Data 15 (1970) 361. Kato, M.; Konishi, H.; Hirata, M.; J. Chem. Eng. Data 15 (1970) 435. Konobeev, B. I.; Lyapin, V. V.; Zh. Prikl. Khim. (Leningrad) 43 (1970) 803. Krichevtsov, B. K.; Komarov, V. M.; Zh. Prikl. Khim. (Leningrad) 43 (1970) 112. Krichevtsov, B. K.; Komarov, V. M.; Zh. Prikl. Khim. (Leningrad) 43 (1970) 703. Kundu, K. K.; Chattopadhyay, P. K.; Jana, D. ; Das, M. N.; J. Chem. Eng. Data 15 (1970) 209. Minowa, Z.; Kawasaki, T.; Inamatsu, T.; Bull. Nat. Res. Lab. Metrol. (Tokyo) No. 21 (1970) 1. Myers, R. S.; Clever, H. L.; J. Chem. Thermodyn. 2 (1970) 53. Nakanishi, K.; Shirai, H.; Bull. Chem. Soc. Jpn. 43 (1970) 1634. Paz Andrade, M. I.; Paz Fernandez, J. M.; Recacho, E.; An. Quim. 66 (1970) 961.

Landolt-Börnstein New Series IV/8G

References 70-puz/bul 70-ras/gaz 70-str/svo 70-sus/hol 70-ver 71-abr/ber 71-bra/joh 71-des/bha-1 71-gol/dob 71-kat/lob 71-nag/oht 71-tha/rao 71-yer/swi 72-bon/pik 72-caz/mar 72-gla/gha 72-nie/nov 72-pol/lu 72-pol/lu-1 72-rak/isa 72-rei/eis 72-udo/maz 73-dak/rao 73-dak/vee 73-daw/new 73-fin 73-gar/paz 73-khi/ale 73-min/rue 73-nag/oht 73-nay/kud 73-svo/ves 73-sza/mys 74-dut/mat 74-jim/paz 74-moo/wel 74-mye/cle 74-paz/rom 74-pur/pol 74-rak/mak 74-rak/mel 74-rak/zlo 74-rao/nai 74-rao/nai-1

Landolt-Börnstein New Series IV/8G

387

Puzitskii, K. V.; Bulanova, T. F.; Bin, Y. Y.; Eidus, Y. T.; Izv. Akad. Nauk SSSR Ser. Khim. (1970) 1872. Rastorguev, Yu. L.; Gazdiev, M. A.; Russ. J. Phys. Chem. (Engl. Transl.) 44 (1970) 1758. Strubl, K.; Svoboda, V.; Holub, R.; Pick, J.; Collect. Czech. Chem. Commun. 35 (1970) 3004. Suska, J.; Holub, R.; Vonka, P.; Pick, J.; Collect. Czech. Chem. Commun. 35 (1970) 385. Verhoeye, L. A. J.; J. Chem. Eng. Data 15 (1970) 222. Abraham, T.; Bery, V.; Kudchadker, A. P.; J. Chem. Eng. Data 16 (1971) 355. Brandreth, D. A.; Johnson, R. E.; J. Chem. Eng. Data 16 (1971) 325. Deshpande, D. D.; Bhalgadde, L. G.; Oswal, S.; Prabhu, C. S.; J. Chem. Eng. Data 16 (1971) 469. Golubev, I. F.; Dobrovolskii, O. A.; Demin, G. P.; Tr. GIAP (1971) 5. Katz, M.; Lobo, P. W.; Minano, A. S.; Solimo, H.; Can. J. Chem. 49 (1971) 2605. Nagata, I.; Ohta, T.; J. Chem. Eng. Data 16 (1971) 164. Thayumanasundaram, R.; Rao, P. B.; J. Chem. Eng. Data 16 (1971) 323. Yergovich, T. W.; Swift, G. W.; Kurata, F.; J. Chem. Eng. Data 16 (1971) 222. Bonnet, J. C.; Pike, F. P.; J. Chem. Eng. Data 17 (1972) 145. Cazaux, L.; Maroni, P.; Bull. Soc. Chim. Fr. (1972) 773. Gladden, J. K.; Ghaffari, F.; J. Chem. Eng. Data 17 (1972) 468. Niepel, W.; Novak, J. P.; Matous, J.; Sobr, J.; Chem. Zvesti 26 (1972) 44. Polak, J.; Lu, B. C. Y.; J. Chem. Eng. Data 17 (1972) 456. Polak, J.; Lu, B. C. Y.; J. Chem. Thermodyn. 4 (1972) 469. Rakhmankulov, D. L.; Isagulyants, V. I.; Zlotskii, S. S.; J. Appl. Chem. USSR (Engl. Transl.) 45 (1972) 2907. Reisler, E.; Eisenberg, H.; J. Chem. Soc., Faraday Trans. 2, 68 (1972) 1001. Udovenko, V. V.; Mazanko, T. F.; Plyngeu, V. Ya.; Zh. Fiz. Khim. 46 (1972) 218. Dakshinamurty, P.; Rao, K. V.; Venkateswara Rao, P.; Chiranjivi, C.; J. Chem. Eng. Data 18 (1973) 39. Dakshinamurty, P.; Veerabhadra Rao, K.; Venkateswara Rao, P.; Chiranjivi, C.; J. Chem. Eng. Data 18 (1973) 39. Dawe, R. A.; Newsham, D. M. T.; Ng, S. B.; J. Chem. Eng. Data 18 (1973) 44. Findenegg, G. H.; Monatsh. Chem. 104 (1973) 998. Garcia, M.; Paz Andrade, M. I.; An. Quim. 69 (1973) 708. Khimenko, M. T.; Aleksandrov, V. V.; Gritsenko, N. N.; Zh. Fiz. Khim. 47 (1973) 2914. Minh, D. C.; Ruel, M.; J. Chem. Eng. Data 18 (1973) 41. Nagata, I.; Ohta, T.; Uchiyama, Y.; J. Chem. Eng. Data 18 (1973) 54. Nayar, S.; Kudchadker, A. P.; J. Chem. Eng. Data 18 (1973) 356. Svoboda, V.; Vesely, F.; Holub, R.; Pick, J.; Collect. Czech. Chem. Commun. 38 (1973) 3539. Szafraniak, K.; Myszkowski, J.; Zielinski, A. Z.; Pyc, W.; Przem. Chem. 52 (1973) 744. Dutta-Choudhury, M. K.; Mathur, H. B.; J. Chem. Eng. Data 19 (1974) 145. Jimenez Cuesta, E.; Paz Andrade, M. I.; An. Quim. 70 (1974) 103. Moore, J. W.; Wellek, R. M.; J. Chem. Eng. Data 19 (1974) 136. Myers, R. S.; Clever, H. L.; J. Chem. Thermodyn. 6 (1974) 949. Paz Andrade, M. I.; Romani, L.; Perez, R.; An. Quim. 70 (1974) 419. Puri, P. S.; Polak, J.; Ruether, J. A.; J. Chem. Eng. Data 19 (1974) 87. Rakhmankulov, D. L.; Maksimova, N. E.; Melikyan, V. R.; Isagulyants, V. I.; J. Appl. Chem. USSR (Engl. Transl.) 47 (1974) 471. Rakhmankulov, D. L.; Melikyan, V. R.; Maksimova, N. E.; Isagulyants, V. I.; J. Appl. Chem. USSR (Engl. Transl.) 47 (1974) 2333. Rakhmankulov, D. L.; Zlotskii, S. S.; Agisheva, S. A.; Maksimova, N. E.; Isagulyants, V. I.; J. Appl. Chem. USSR (Engl. Transl.) 47 (1974) 1472. Rao, M. V. P.; Naidu, P. R.; Can. J. Chem. 52 (1974) 788. Rao, M. V. P.; Naidu, P. R.; J. Chem. Thermodyn. 6 (1974) 1195.

388 74-wol/ska 75-esp/man 75-hsu/cle 75-khi/gri 75-kub/tan 75-lee/che 75-mat/fer 75-mus/ver 75-nak/kom 75-tok 76-for/ben 76-hal/ell 76-hon/sin 76-kat/nit 76-kow/kas 76-nag/oht 76-sri/kul 76-sub/nai 76-tri/kri 76-wes 76-wes-1 77-bel/bub 77-cam/sch 77-gov/and-1 77-gup/han 77-hwa/rob 77-tan/yam 77-tre/ben 77-zhu/zhu-2 78-amb/cou-1 78-apa/ker-2 78-ast 78-dap/don 78-fro/ers-1 78-jel/leo 78-mus/kan 78-nit/fuj 78-ovc/kry 78-paz/gar 78-red/nai-1 78-sac/pes 78-tre/ben 79-bal/fri 79-cha/ses-1

References Wollmann, H.; Skaletki, B.; Schaaf, A.; Pharmazie 29 (1974) 708. Espanol, M.; Manisse, A.; Beaudoin, M. T.; C. R. Hebd. Seances Acad. Sci. C 281 (1975) 445. Hsu, K.-Y.; Clever, H. L.; J. Chem. Eng. Data 20 (1975) 268. Khimenko, M. T.; Gritsenko, N. N.; Tsybizova, L. P.; Bezpalyi, B. N.; Russ. J. Phys. Chem. 49 (1975) 146. Kubota, H.; Tanaka, Y.; Makita, T.; Kagaku Kogaku Ronbunshu 1 (1975) 176. Leets, K. V.; Chernyshev, V. O.; Rang, K. A.; Erm, A. Y.; Zh. Org. Khim. 11 (1975) 1811. Mato, F.; Fernandez-Polonco, F.; An. Quim. 71 (1975) 815. Mussche, M. J.; Verhoeye, L. A. J.; J. Chem. Eng. Data 20 (1975) 46. Nakajima, T.; Komatsu, T.; Nakagawa, T.; Bull. Chem. Soc. Jpn. 48 (1975) 783. Tokunaga, J.; J. Chem. Eng. Data 20 (1975) 41. Fortier, J.-L.; Benson, G. C.; Picker, P.; J. Chem. Thermodyn. 8 (1976) 289. Hales, J. L.; Ellender, J. H.; J. Chem. Thermodyn. 8 (1976) 1177. Hon, H. C.; Singh, R. P.; Kudchadker, A. P.; J. Chem. Eng. Data 21 (1976) 430. Katayama, T.; Nitta, T.; J. Chem. Eng. Data 21 (1976) 194. Kowalski, B.; Kasprzycka-Guttman, T.; Orszagh, A.; Rocz. Chem. 50 (1976) 1445. Nagata, I.; Ohta, T.; Ogura, M.; Yasuda, S.; J. Chem. Eng. Data 21 (1976) 310. Srinivasan, D.; Kulkarni, P. L.; Chem. Eng. World 11(12) (1976) 63. Subramanyam Reddy, K.; Naidu, P. R.; J. Chem. Thermodyn. 8 (1976) 1208. Tripathi, R. P.; Krishna, S.; Gulati, I. B.; J. Chem. Eng. Data 21 (1976) 44. Westmeier, S.; Chem. Tech. (Leipzig) 28 (1976) 350. Westmeier, S.; Chem. Tech. (Leipzig) 28 (1976) 480. Belousov, V. P.; Bubnov, V. I.; Pfestorf, R.; Schumichen, A.; Z. Chem. 17 (1977) 382. Cammenga, H. K.; Schulze, F. W.; Theuerl, W.; J. Chem. Eng. Data 22 (1977) 131. Govindaswamy, S.; Andiappan, A. N.; Lakshmanan, S. M.; J. Chem. Eng. Data 22 (1977) 264. Gupta, A. C.; Hanks, R. W.; Thermochim. Acta 21 (1977) 143. Hwang, S.-C.; Robinson, R. L.; J. Chem. Eng. Data 22 (1977) 319. Tanaka, Y.; Yamamoto, T.; Satomi, Y.; Kubota, H.; Makita, T.; Rev. Phys. Chem. Jpn. 47 (1977) 12. Treszczanowicz, A. J.; Benson, G. C.; J. Chem. Thermodyn. 9 (1977) 1189. Zhuravleva, I. K.; Zhuravlev, E. F.; J. Gen. Chem. USSR (Engl. Transl.) 47 (1977) 1774. Ambrose, D.; Counsell, J. F.; Lawrenson, I. J.; Lewis, G. B.; J. Chem. Thermodyn. 10 (1978) 1033. Apaev, T. A.; Kerimov, A. M.; Imanova, I. G.; High Temp. 16 (1978) 575. Astrup, E. E.; Acta Chem. Scand., Ser. A 32 (1978) 115. D'Aprano, A.; Donato, I. D.; Caponetti, E.; Agrigento, V.; Gazz. Chim. Ital. 108 (1978) 601. Frolova, E. A.; Ershova, T. P.; Ustavshchikov, B. F.; Kiselev, V. Ya.; J. Appl. Chem. USSR (Engl. Transl.) 51 (1978) 2251. Jelinek, R. M.; Leopold, H.; Monatsh. Chem. 109 (1978) 387. Musavirov, R. S.; Kantor, E. A.; Rakhmankulov, D. L.; J. Appl. Chem. USSR (Engl. Transl.) 51 (1978) 2184. Nitta, T.; Fujio, J.; Katayama, T.; J. Chem. Eng. Data 23 (1978) 157. Ovcschinnikova, T. F.; Kryukov, S. I.; Simanov, N. A.; Farberov, M. I.; Neftekhimiya 18 (1978) 80. Paz Andrade, M. I.; Garcia, M.; Baluja, M. C.; Sanchez Bana, M. E.; Acta Cient. Compostelana 15 (1978) 33. Subramanyam Reddy, K.; Naidu, P. R.; J. Chem. Thermodyn. 10 (1978) 201. Sachek, A. I.; Peshchenko, A. D.; Andreevskii, D. N.; Vestsi Akad. Navuk BSSR Ser. Khim. Navuk (1978) 124. Treszczanowicz, A. J.; Benson, G. C.; J. Chem. Thermodyn. 10 (1978) 967. Balish, M.; Fried, V.; J. Chem. Eng. Data 24 (1979) 91. Chandrashekara, M. N.; Seshadri, D. N.; Indian J. Technol. 17 (1979) 243.

Landolt-Börnstein New Series IV/8G

References 79-dia/tar 79-ern/gli 79-gyl/apa 79-jim/paz 79-kiy/ben 79-sah/hay 79-sin/siv 79-sub/rao 79-tho/nag 79-zel/hub 80-arc/bla 80-ben/kiy 80-bru 80-cha/ses 80-edu/boy 80-fuk/ogi 80-kas/izy 80-mar/ric 80-oza/ooy 80-pik 80-rig/ube 80-sue/mul 80-tre/ben 80-yos/tak 80-yu/ish 81-ben/han 81-han/hal 81-joo/arl 81-kim/ben 81-kiy/ben 81-kor/kov 81-kum/pra 81-nai/nai 81-nar/dha 81-oht/koy 81-sjo/dyh 81-tas/ara 81-tre/kiy 81-won/chu 82-aww/pet 82-ber/rog-1 82-dap/don 82-diz/mar 82-dom/rat 82-kar/red 82-kat/wat 82-man/les

Landolt-Börnstein New Series IV/8G

389

Diaz Pena, M.; Tardajos, G.; J. Chem. Thermodyn. 11 (1979) 441. Ernst, S.; Glinski, J.; Jezowska-Trzebiatowska, B.; Acta Phys. Pol., A 55 (1979) 501. Gylmanov, A. A.; Apaev, T. A.; Akhmedov, L. A.; Lipovetskii, S. I.; Izv. Vyssh. Uchebn. Zaved., Neft Gaz 22 (1979) 55. Jimenez Cuesta, E.; Paz Andrade, M. I.; Casanova, C.; J. Chim. Phys. Phys.-Chim. Biol. 76 (1979) 46. Kiyohara, O.; Benson, G. C.; J. Chem. Thermodyn. 11 (1979) 861. Sahgal, A.; Hayduk, W.; J. Chem. Eng. Data 24 (1979) 222. Singh, S.; Sivanarayana, K.; Kushwaha, R.; Prakash, S.; J. Chem. Eng. Data 24 (1979) 279. Subba Rao, D.; Rao, K. V.; Ravi Prasad, A.; Chiranjivi, C.; J. Chem. Eng. Data 24 (1979) 241. Thorat, R. T.; Nageshwar, G. D.; Mene, P. S.; J. Chem. Eng. Data 24 (1979) 270. Zeltner, P.; Huber, G. A.; Peters, R.; Tatrai, F.; Boksanyi, L.; Kovats, E. S.; Helv. Chim. Acta 62 (1979) 2495 Arce, A.; Blanco, A.; Antorrena, G.; Quintela, M. D.; An. Quim., Ser. A 76 (1980) 405. Benson, G. C.; Kiyohara, O.; J. Solution Chem. 9 (1980) 791. Brunner, E.; J. Chem. Thermodyn. 12 (1980) 993. Chandrashekara, M. N.; Seshadri, D. N.; J. Chem. Eng. Data 25 (1980) 124. Eduljee, G. H.; Boyes, A. P.; J. Chem. Eng. Data 25 (1980) 249. Fukuchi, K.; Ogiwara, K.; Yonezawa, S.; Arai, Y.; Kogaku Shuho - Kyushu Daigaku 53 (1980) 187. Kasprzycka-Guttman, T.; Izycka, K.; Czelej, M.; Pol. J. Chem. 54 (1980) 1775. Marsh, K. N.; Richards, A. E.; Aust. J. Chem. 33 (1980) 2121. Ozawa, S.; Ooyatsu, N.; Yamabe, M.; Honmo, S.; Ogino, Y.; J. Chem. Thermodyn. 12 (1980) 229. Pikkarainen, L.; Finn. Chem. Lett. No. 7-8 (1980) 185. Riggio, R.; Ubeda, M. H.; Ramos, J. F.; Martinez, H. E.; J. Chem. Eng. Data 25 (1980) 318. Suehnel, K.; Muller, S.; Z. Phys. Chem. (Leipzig) 261 (1980) 60. Treszczanowicz, A. J.; Benson, G. C.; J. Chem. Thermodyn. 12 (1980) 173. Yoshikawa, Y.; Takagi, A.; Kato, M.; J. Chem. Eng. Data 25 (1980) 344. Yu, J.-M.; Ishikawa, T.; Lu, B. C. Y.; J. Chem. Thermodyn. 12 (1980) 57. Benson, G. C.; Handa, Y. P.; J. Chem. Thermodyn. 13 (1981) 887. Handa, Y. P.; Halpin, C. J.; Benson, G. C.; J. Chem. Thermodyn. 13 (1981) 875. Joo, H.-J.; Arlt, W.; J. Chem. Eng. Data 26 (1981) 138. Kimura, F.; Benson, G. C.; J. Chem. Eng. Data 26 (1981) 317. Kiyohara, O.; Benson, G. C.; J. Chem. Eng. Data 26 (1981) 263. Korosi, G.; Kovats, E.; J. Chem. Eng. Data 26 (1981) 323. Kumar, A.; Prakash, O.; Prakash, S.; J. Chem. Eng. Data 26 (1981) 64. Naidu, G. R.; Naidu, P. R.; J. Chem. Eng. Data 26 (1981) 197. Narayanaswamy, G.; Dharmaraju, G.; Raman, G. K.; J. Chem. Thermodyn. 13 (1981) 327. Ohta, T.; Koyabu, J.; Nagata, I.; Fluid Phase Equilib. 7 (1981) 65. Sjoblom, J.; Dyhr, H.; Hansen O.; Finn. Chem. Lett. (1981) 110 Tashima, Y.; Arai, Y.; Mem. Fac. Eng., Kyushu Univ. 41 (1981) 217. Treszczanowicz, A. J.; Kiyohara, O.; Benson, G. C.; J. Chem. Thermodyn. 13 (1981) 253. Won, Y. S.; Chung, D. K.; Mills, A. F.; J. Chem. Eng. Data 26 (1981) 140. Awwad, A. M.; Pethrick, R. A.; J. Chem. Soc., Faraday Trans. 1 78 (1982) 3203. Berro, C.; Rogalski, M.; Peneloux, A.; J. Chem. Eng. Data 27 (1982) 352. D'Aprano, A.; Donato, I. D.; Agrigento, V.; J. Solution Chem. 11 (1982) 259. Dizechi, M.; Marschell, E.; J. Chem. Eng. Data 27 (1982) 358. Domonkos, L.; Ratkovics, F.; Monatsh. Chem. 113 (1982) 1119. Karunakar, J.; Reddy, K. D.; Rao, M. V. P.; J. Chem. Eng. Data 27 (1982) 346. Katayama, H.; Watanabe, I.; J. Chem. Eng. Data 27 (1982) 91. Mandik, L.; Lesek, F.; Coll. Czech. Chem. Comm. 47 (1982) 1686.

390 82-nai/nai 82-ort 82-sch/pol 82-sin/sin 82-tre/han 82-ven/dha 82-zak 83-alb/edg 83-dap/del 83-fuk/ogi 83-gop/rao 83-hal/gun 83-kim/ben 83-lin 83-pik-1 83-pik-2 83-rau/ste 83-tri 83-wec 83-wec/byl 84-ber/pen 84-bra/pin 84-cer/bou 84-eas/woo 84-idr/fre 84-kim/ben 84-kum/ben 84-ort/ang 84-ped/sal 84-sak/nak 85-bel/ber 85-chi/lin 85-dap/don 85-dri/ras 85-fer/ber 85-fer/pin 85-kov/svo 85-kum/ben 85-les/eic 85-mat/ben 85-mat/ben-1 85-nag 85-nag-1 85-nag-2 85-nag-3 85-ogi/ara 85-ort

References Naidu, G. R.; Naidu, P. R.; Indian J. Pure Appl. Phys. 20 (1982) 313. Ortega, J.; J. Chem. Eng. Data 27 (1982) 312. Schroeder, M. R.; Poling, B. E.; Manley, D. B.; J. Chem. Eng. Data 27 (1982) 256. Singh, R. P.; Sinha, C. P.; J. Chem. Eng. Data 27 (1982) 283. Treszczanowicz, A. J.; Handa, Y. P.; Benson, G. C.; J. Chem. Thermodyn. 14 (1982) 871. Venkateswarlu, P.; Dharmaraju, G.; Raman, G. K.; Acoust. Lett. 6 (1982) 1. Zakharyaev, Z. R.; Inzh.-Fiz. Zh. 43 (1982) 796. Albright, J. G.; Edge, A. V. J.; Mills, R.; J. Chem. Soc., Faraday Trans. 1 79 (1983) 1327. D'Aprano, A.; De Lisi, R.; Donato, I. D.; J. Solution Chem. 12 (1983) 383. Fukuchi, K.; Ogiwara, K.; Tashima, Y.; Yonezawa, S.; Ube Kogyo Koto Senmon Gakko Kenkyu Hokoku 29 (1983) 93. Gopal, K.; Rao, N. P.; Acustica 54 (1983) 115. Hales, J. L.; Gundry, H. A.; Ellender, J. H.; J. Chem. Thermodyn. 15 (1983) 211. Kimura, F.; Benson, G. C.; J. Chem. Eng. Data 28 (1983) 157. Linek, J.; Collect. Czech. Chem. Commun. 48 (1983) 2446. Pikkarainen, L.; Finn. Chem. Lett. No. 3-4 (1983) 63. Pikkarainen, L.; J. Chem. Eng. Data 28 (1983) 344. Rauf, M. A.; Stewart, G. H.; Farhat-Aziz; J. Chem. Eng. Data 28 (1983) 324. Triday, J. O.; J. Chem. Eng. Data 28 (1983) 307. Weclawski, J.; Fluid Phase Equilib. 12 (1983) 155. Weclawski, J.; Bylicki, A.; Fluid Phase Equilib. 12 (1983) 143. Berro, C.; Peneloux, A.; J. Chem. Eng. Data 29 (1984) 206. Bravo, R.; Pintos, M.; Baluja, M. C.; Paz Andrade, M. I.; Roux-Desgranges, G.; Grolier, J.-P. E.; J. Chem. Thermodyn. 16 (1984) 73. Cervenkova, I.; Boublik, T.; J. Chem. Eng. Data 29 (1984) 425. Easteal, A. J.; Woolf, L. A.; J. Chem. Thermodyn. 16 (1984) 391. Idriss-Ali, K. M.; Freeman, G. R.; Can. J. Chem. 62 (1984) 2217. Kimura, F.; Benson, G. C.; Fluid Phase Equilib. 16 (1984) 77. Kumaran, M. K.; Benson, G. C.; J. Chem. Thermodyn. 16 (1984) 175. Ortega, J.; Angulo, M. C.; J. Chem. Eng. Data 29 (1984) 340. Pedrosa, G. C.; Salas, J. A.; Davolio, F.; Katz, M.; An. Asoc. Quim. Argent. 72 (1984) 541. Sakurai, M.; Nakagawa, T.; J. Chem. Thermodyn. 16 (1984) 171. Belousov, V. P.; Beregovykh, V. V.; Gurarii, L. L.; Vses. Konf. po Termodinamike Organicheskikh Soyedinenii, 4th, Kuibyshev (1985) 100. Chiu, R. M.-H.; Lin, H. B.; Kan, P. Y.; J. Chin. Inst. Chem. Eng. 16 (1985) 307. D'Aprano, A.; Donato, I. D.; D'Arrigo, G.; Bertolini, D.; Cassettari, M.; Salvetti, G.; Mol. Phys. 55 (1985) 475. Dribika, M. M.; Rashed, I. G.; Biddulph, M. W.; J. Chem. Eng. Data 30 (1985) 146. Fernandez, J.; Berro, C.; Paz Andrade, M. I.; Fluid Phase Equilib. 20 (1985) 145. Fernandez, J.; Pintos, M.; Baluja, M. C.; Jimenez Cuesta, E.; Paz Andrade, M. I.; J. Chem. Eng. Data 30 (1985) 318. Kovac, A.; Svoboda, J.; Ondrus, I.; Chem. Zvesti 39 (1985) 729. Kumaran, M. K.; Benson, G. C.; J. Chem. Thermodyn. 17 (1985) 699. Lesek, F.; Eichler, J.; Balcar, M.; Collect. Czech. Chem. Commun. 50 (1985) 153. Mato, F.; Benito, G. G.; An. Quim., Ser. A 81 (1985) 116. Mato, F.; Benito, G. G.; Sobron, F.; An. Quim., Ser. A 81 (1985) 400. Nagata, I.; J. Chem. Eng. Data 30 (1985) 201. Nagata, I.; J. Chem. Eng. Data 30 (1985) 363. Nagata, I.; Fluid Phase Equilib. 24 (1985) 279. Nagata, I.; Fluid Phase Equilib. 19 (1985) 13. Ogiwara, K.; Arai, Y.; Saito, S.; J. Chem. Eng. Jpn. 18 (1985) 273. Ortega, J.; J. Chem. Eng. Data 30 (1985) 5.

Landolt-Börnstein New Series IV/8G

References 85-ort-1 85-ort/paz-1 85-ort/paz-2 85-ped/dav 85-rao/red 85-sar/paz 85-sin/sin 85-sin/sin-1 85-tre/ben 85-wie/sip 85-zhu 85-zhu/dur 86-ash/sri 86-bae 86-ber/wec 86-ber/wec-1 86-cha/lam 86-dew/meh 86-hei/sch 86-hne/cib 86-kar/cam 86-lep/mat 86-mah/daw 86-miy/hay 86-mou/nai 86-oga/mur 86-ort/paz 86-ort/paz-1 86-ort/pen 86-rig/mar 86-san/sha 86-sin/sin 86-tan/toy 86-wag/hei 86-zha/ben-1 87-ber-1 87-ber-2 87-ber-3 87-ber-4 87-ber-8 87-ber-9 87-dew/meh 87-fer/ber 87-isl/qua 87-kri/cho 87-kub/tan 87-mou

Landolt-Börnstein New Series IV/8G

391

Ortega, J.; J. Chem. Eng. Data 30 (1985) 462. Ortega, J.; Paz Andrade, M. I.; Rodriguez-Nunez, E.; Romani, L.; Aust. J. Chem. 38 (1985) 1435. Ortega, J.; Paz Andrade, M. I.; Bravo, R.; J. Chem. Thermodyn. 17 (1985) 1199. Pedrosa, G. C.; Davolio, F.; Schaefer, C. O.; Katz, M.; Rev. Latinoam. Ing. Quim. Quim. Apl. 15 (1985) 189. Rao, K. P. C.; Reddy, K. S.; Thermochim. Acta 91 (1985) 321. Sarmiento, F.; Paz Andrade, M. I.; Fernandez, J.; Bravo, R.; Pintos, M.; J. Chem. Eng. Data 30 (1985) 321. Singh, R. P.; Sinha, C. P.; J. Chem. Eng. Data 30 (1985) 38. Singh, R. P.; Sinha, C. P.; J. Chem. Eng. Data 30 (1985) 470. Treszczanowicz, A. J.; Benson, G. C.; J. Chem. Thermodyn. 17 (1985) 123. Wieczorek, S. A.; Sipowska, J. T.; J. Chem. Thermodyn. 17 (1985) 255. Zhuravleva, I. K.; Zh. Obshch. Khim. 55 (1985) 1685. Zhuravlev, V. I.; Durov, V. A.; Usacheva, T. M.; Shakhparonov, M. I.; Zh. Fiz. Khim. 59 (1985) 1677 Ashraf, S. M.; Srivastava, R.; Hussain, A.; J. Chem. Eng. Data 31 (1986) 100. Baev, A. A.; Termodin. Org. Soedin. (1986) 74. Berro, C.; Weclawski, J.; Int. DATA Ser., Sel. Data Mixtures Ser. A No. 3 (1986) 224. Berro, C.; Weclawski, J.; Int. DATA Ser., Sel. Data Mixtures Ser. A No. 3 (1986) 221. Chauhdry, M. S.; Lamb, J. A.; J. Chem. Thermodyn. 18 (1986) 665. Dewan, R. K.; Mehta, S. K.; J. Chem. Thermodyn. 18 (1986) 697. Heintz, A.; Schmittecker, B.; Wagner, D.; Lichtenthaler, R. N.; J. Chem. Eng. Data 31 (1986) 487. Hnedkovsky, L.; Cibulka, I.; J. Chem. Thermodyn. 18 (1986) 331. Kartzmark, E. M.; Campbell, A. N.; J. Chem. Eng. Data 31 (1986) 241. Lepori, L.; Matteoli, E.; J. Chem. Thermodyn. 18 (1986) 13. Mahers, E. G.; Dawe, R. A.; J. Chem. Eng. Data 31 (1986) 28. Miyano, Y.; Hayduk, W.; J. Chem. Eng. Data 31 (1986) 81. Mouli, J. C.; Naidu, P. R.; Choudary, N. V.; J. Chem. Eng. Data 31 (1986) 493. Ogawa, H.; Murakami, S.; Thermochim. Acta 109 (1986) 145. Ortega, J.; Paz Andrade, M. I.; Rodriguez-Nunez, E.; J. Chem. Eng. Data 31 (1986) 336. Ortega, J.; Paz Andrade, M. I.; J. Chem. Eng. Data 31 (1986) 231. Ortega, J.; Pena, J. A.; de Alfonso, C.; J. Chem. Eng. Data 31 (1986) 339. Riggio, R.; Martinez, H. E.; Solimo, H. N.; J. Chem. Eng. Data 31 (1986) 235. Sandhu, J. S.; Sharma, A. K.; Wadi, R. K.; J. Chem. Eng. Data 31 (1986) 152. Singh, R. P.; Sinha, C. P.; Singh, B. N.; J. Chem. Eng. Data 31 (1986) 107. Tanaka, R.; Toyama, S.; Murakami, S.; J. Chem. Thermodyn. 18 (1986) 63. Wagner, D.; Heintz, A.; J. Chem. Eng. Data 31 (1986) 483. Zhang, D.; Benson, G. C.; Kumaran, M. K.; Lu, B. C. Y.; J. Chem. Thermodyn. 18 (1986) 149. Berro, C.; Int. DATA Ser., Sel. Data Mixtures Ser. A No. 2 (1987) 96. Berro, C.; Int. DATA Ser., Sel. Data Mixtures Ser. A No. 2 (1987) 85. Berro, C.; Int. DATA Ser., Sel. Data Mixtures Ser. A No. 1 (1987) 64. Berro, C.; Int. DATA Ser., Sel. Data Mixtures Ser. A No. 2 (1987) 87. Berro, C.; Int. DATA Ser., Sel. Data Mixtures Ser. A No. 1 (1987) 62. Berro, C.; Int. DATA Ser., Sel. Data Mixtures Ser. A No. 1 (1987) 63. Dewan, R. K.; Mehta, S. K.; J. Chem. Thermodyn. 19 (1987) 819. Fernandez, J.; Berro, C.; Peneloux, A.; J. Chem. Eng. Data 32 (1987) 17. Islam, M. R.; Quadri, S. K.; Thermochim. Acta 115 (1987) 335. Krishnaiah, A.; Choudary, N. V.; J. Chem. Eng. Data 32 (1987) 196. Kubota, H.; Tanaka, Y.; Makita, T.; Int. J. Thermophys. 8 (1987) 47. Mousa, A. H. N.; J. Chem. Eng. Jpn. 20 (1987) 635.

392 87-oga/mur 87-ogi/ara 87-pap/pap 87-pik 87-rat/sin-3 88-bag/gur 88-cab/bar 88-cac/cos 88-cze/zyw 88-dou/pal 88-jad/fra 88-kim/mar 88-nag 88-nag-1 88-nag-2 88-nag-4 88-oka/oga 88-ort/gar 88-ort/mat 88-sak 88-sip/wie 88-sun/bis 88-sun/sch-1 88-sun/ten 88-tan/luo 89-ala/sal 89-dew/gup 89-kac/rad 89-kat/tan 89-mat/mak-1 89-nao/sur 89-ort/sus 89-pae/con 89-sin/sin 89-sus/ort 89-taw/tej 89-vij/nai 90-apa/gyl 90-bar/paz 90-cha/kat 90-klo/pal 90-lee/hon 90-mal/rao 90-sri/nai 90-sun/sch-1 90-vij/nai 91-ace/ped-1 91-cab/bel

References Ogawa, H.; Murakami, S.; J. Solution Chem. 16 (1987) 315. Ogiwara, K.; Arai, Y.; Netsu Bussei 1 (1987) 52. Papanastasiou, G. E.; Papoutsis, A. D.; Kokkinidis, I.; J. Chem. Eng. Data 32 (1987) 377. Pikkarainen, L.; J. Chem. Eng. Data 32 (1987) 429. Rattan, V. K.; Singh, S.; Sethi, B. P. S.; Raju, K. S. N.; J. Chem. Thermodyn. 19 (1987) 535. Baglai, A. K.; Gurarii, L. L.; Kuleshov, G. G.; J. Chem. Eng. Data 33 (1988) 512. Cabezas, J. L.; Barcena, L. A.; Coca, J.; Cockrem, M.; J. Chem. Eng. Data 33 (1988) 435. Caceres Alonso, M.; Costas, M.; Andreoli-Ball, L.; Patterson, D.; Can. J. Chem. 66 (1988) 989. Czechowski, G.; Zywucki, B.; Jadzyn, J.; J. Chem. Eng. Data 33 (1988) 55. Douheret, G.; Pal, A.; J. Chem. Eng. Data 33 (1988) 40. Jadot, R.; Fraiha, M.; J. Chem. Eng. Data 33 (1988) 237. Kim, E. S.; Marsh, K. N.; J. Chem. Eng. Data 33 (1988) 288. Nagata, I.; Thermochim. Acta 126 (1988) 107. Nagata, I.; Thermochim. Acta 127 (1988) 109. Nagata, I.; Thermochim. Acta 127 (1988) 337. Nagata, I.; J. Chem. Eng. Data 33 (1988) 286. Okano, T.; Ogawa, H.; Murakami, S.; Can. J. Chem. 66 (1988) 713. Ortega, J.; Garcia, J. D.; Can. J. Chem. 66 (1988) 1520. Ortega, J.; Matos, J. S.; Pena, J. A.; Paz Andrade, M. I.; Pias, L.; Fernandez, J.; Thermochim. Acta 131 (1988) 57. Sakurai, M.; J. Solution Chem. 17 (1988) 267. Sipowska, J. T.; Wieczorek, S. A.; J. Chem. Thermodyn. 20 (1988) 333. Sun, T.; Biswas, S. N.; Trappeniers, N. J.; Ten Seldam, C. A.; J. Chem. Eng. Data 33 (1988) 395. Sun, T. F.; Schouten, J. A.; Trappeniers, N. J.; Biswas, S. N.; J. Chem. Thermodyn. 20 (1988) 1089. Sun, T. F.; Ten Seldam, C. A.; Kortbeek, P. J.; Trappeniers, N. J.; Biswas, S. N.; Phys. Chem. Liq. 18 (1988) 107. Tanaka, R.; Luo, B.; Benson, G. C.; Lu, B. C. Y.; Thermochim. Acta 127 (1988) 15. Al-Azzawi, S. F.; Salman, M. A.; Fluid Phase Equilib. 45 (1989) 95. Dewan, R. K.; Gupta, S. P.; Mehta, S. K.; J. Solution Chem. 18 (1989) 13. Kaczmarek, B.; Radecki, A.; J. Chem. Eng. Data 34 (1989) 195. Kato, M.; Tanaka, H.; J. Chem. Eng. Data 34 (1989) 203. Matsuo, S.; Makita, T.; Int. J. Thermophys. 10 (1989) 885. Naorem, H.; Suri, S. K.; J. Chem. Eng. Data 34 (1989) 395. Ortega, J.; Susial, P.; Can. J. Chem. 67 (1989) 1120. Paez, S.; Contreras-Slotosch, M.; J. Chem. Eng. Data 34 (1989) 455. Singh, R. P.; Sinha, C. P.; Das, J. C.; Ghosh, P.; J. Chem. Eng. Data 34 (1989) 335. Susial, P.; Ortega, J.; de Alfonso, C.; Alonso, C.; J. Chem. Eng. Data 34 (1989) 247. Tawfik, W. Y.; Teja, A. S.; Chem. Eng. Sci. 44 (1989) 921. Vijayalakshmi, T. S.; Naidu, P. R.; J. Chem. Eng. Data 34 (1989) 413 Apaev, T. A.; Gylmanov, A. A.; Izv. Vyssh. Uchebn. Zaved., Neft Gaz 33 (1990) 22. Bartolome, A. L.; Pazos, C.; Coca, J.; J. Chem. Eng. Data 35 (1990) 285. Chaudhari, S. K.; Katti, S. S.; Thermochim. Acta 158 (1990) 99. Klofutar, C.; Paljk, S.; Domanska, U.; Thermochim. Acta 158 (1990) 301. Lee, H.; Hong, W. H.; Kim, H.; J. Chem. Eng. Data 35 (1990) 371. Mallu, B. V.; Rao, Y. V. C.; J. Chem. Eng. Data 35 (1990) 444. Srinivasulu, U.; Naidu, P. R.; J. Chem. Eng. Data 35 (1990) 33. Sun, T. F.; Schouten, J. A.; Biswas, S. N.; Ber. Bunsen-Ges. Phys. Chem. 94 (1990) 528. Vijayalakshmi, T. S.; Naidu, P. R.; J. Chem. Eng. Data 35 (1990) 338. Acevedo, I. L.; Pedrosa, G. C.; Arancibia, E. L.; Katz, M.; J. Chem. Eng. Data 36 (1991) 137. Cabezas, J. L.; Beltran, S.; Coca, J.; J. Chem. Eng. Data 36 (1991) 184.

Landolt-Börnstein New Series IV/8G

References 91-dou/pal 91-fen/wan 91-gar/her 91-kat/tan 91-ram/muk 91-sun/sch 91-yos/kat 92-ard/say-1 92-kum/sre 92-lie/sen-1 92-sun/dig 92-tan/mur 93-ami/ara 93-ami/rai 93-chi/pro 93-gar/ban-1 93-kum/moc 93-yan/mae 94-ben/car 94-gil 94-hia/tak 94-hia/tak-1 94-kim/lee 94-kum/nai 94-kum/nai-1 94-pap/pan 94-pap/pan-1 94-rom/pel 94-sin/kal 94-tar/jun 94-ven/ven 94-yu/tsa 94-yu/tsa-1 95-arc/bla 95-cas/cal 95-fra/jim 95-fra/men 95-hia/tak 95-hia/tak-1 95-kum/rao-1 95-org/igl 95-red/ram-1 95-sen/say 96-bha/mak 96-dej/gon-1 96-dom/rod

Landolt-Börnstein New Series IV/8G

393

Douheret, G.; Pal, A.; Hoiland, H.; Anowi, O.; Davis, M. I.; J. Chem. Thermodyn. 23 (1991) 569. Feng, H.; Wang, Y.; Shi, J.; Benson, G. C.; Lu, B. C. Y.; J. Chem. Thermodyn. 23 (1991) 169. Garcia, B.; Herrera, C.; Leal, J. M.; J. Chem. Eng. Data 36 (1991) 269. Kato, M.; Tanaka, H.; Yoshikawa, H.; J. Chem. Eng. Data 36 (1991) 387. Ramprasad, G.; Mukherjee, A. K.; Das, T. R.; J. Chem. Eng. Data 36 (1991) 124. Sun, T. F.; Schouten, J. A.; Biswas, S. N.; Int. J. Thermophys. 12 (1991) 381. Yoshikawa, H.; Kato, M.; J. Chem. Eng. Data 36 (1991) 57. Arda, N.; Sayar, A. A.; Fluid Phase Equilib. 73 (1992) 129. Kumar, V. C.; Sreenivasulu, B.; Naidu, P. R.; J. Chem. Eng. Data 37 (1992) 71. Liew, K. Y.; Seng, C. E.; Ng, B. H.; J. Solution Chem. 21 (1992) 1177. Sun, T.; DiGuilio, R. M.; Teja, A. S.; J. Chem. Eng. Data 37 (1992) 246. Tanaka, H.; Muramatsu, T.; Kato, M.; J. Chem. Eng. Data 37 (1992) 164. Aminabhavi, T. M.; Aralaguppi, M. I.; Harogoppad, S. B.; Balundgi, R. H.; J. Chem. Eng. Data 38 (1993) 31. Aminabhavi, T. M.; Raikar, S. K.; J. Chem. Eng. Data 38 (1993) 310. Chiavone-Filho, O.; Proust, P.; Rasmussen, P.; J. Chem. Eng. Data 38 (1993) 128. Garg, S. K.; Banipal, T. S.; Ahluwalia. J. C.; J. Chem. Eng. Data 38 (1993) 227. Kumagai, A.; Mochida, H.; Takahashi, S.; Int. J. Thermophys. 14 (1993) 45. Yanes, C.; Maestre, A.; Perez-Tejeda, P.; Calvente, J. J.; J. Chem. Eng. Data 38 (1993) 512. Benito, G. G.; Carton, A.; Uruena, M. A.; J. Chem. Eng. Data 39 (1994) 249. Gillis, K. A.; Int. J. Thermophys. 15 (1994) 821. Hiaki, T.; Takahashi, K.; Tsuji, T.; Hongo, M.; Kojima, K.; J. Chem. Eng. Data 39 (1994) 602. Hiaki, T.; Takahashi, K.; Tsuji, T.; Hongo, M.; Kojima, K.; J. Chem. Eng. Data 39 (1994) 605. Kim, K.-J.; Lee, C.-H.; Ryu, S.-K.; J. Chem. Eng. Data 39 (1994) 228. Kumar, K. S.; Naidu, P. R.; J. Chem. Eng. Data 39 (1994) 5. Kumar, K. S.; Naidu, P. R.; Acree, W. E.; J. Chem. Eng. Data 39 (1994) 2. Papaioannou, D.; Panayiotou, C. G.; J. Chem. Eng. Data 39 (1994) 463. Papaioannou, D.; Panayiotou, C. G.; J. Chem. Eng. Data 39 (1994) 457. Romani, L.; Peleteiro, J.; Iglesias, T. P.; Carballo, E.; Escudero, R.; Legido, J. L.; J. Chem. Eng. Data 39 (1994) 19. Singh, K. C.; Kalra, K. C.; Maken, S.; Yadav, B. L.; J. Chem. Eng. Data 39 (1994) 241. Tardajos, G.; Junquera, E.; Aicart, E.; J. Chem. Eng. Data 39 (1994) 349. Venkatesu, P.; Venkatesulu, D.; Rao, M. V. P.; J. Chem. Eng. Data 39 (1994) 140. Yu, C. H.; Tsai, F. N.; J. Chem. Eng. Data 39 (1994) 125. Yu, C. H.; Tsai, F. N.; J. Chem. Eng. Data 39 (1994) 441. Arce, A.; Blanco, A.; Souza, P.; Vidal, I.; J. Chem. Eng. Data 40 (1995) 225. Castro, I.; Calvo, E.; Bravo, R.; Pintos, M.; Amigo, A.; J. Chem. Eng. Data 40 (1995) 230. Franjo, C.; Jimenez Cuesta, E.; Iglesias, T. P.; Legido, J. L.; Paz Andrade, M. I.; J. Chem. Eng. Data 40 (1995) 68. Franjo, C.; Menaut, C. P.; Jimenez Cuesta, E.; Legido, J. L.; Paz Andrade, M. I.; J. Chem. Eng. Data 40 (1995) 992. Hiaki, T.; Takahashi, K.; Tsuji, T.; Hongo, M.; Kojima, K.; J. Chem. Eng. Data 40 (1995) 274. Hiaki, T.; Takahashi, K.; Tsuji, T.; Hongo, M.; Kojima, K.; J. Chem. Eng. Data 40 (1995) 271. Kumar, R. V.; Rao, M. A.; Prasad, D. H. L.; Rao, M. V.; J. Chem. Eng. Data 40 (1995) 1056 Orge, B.; Iglesias, M.; Tojo, J.; J. Chem. Eng. Data 40 (1995) 260. Reddy, V. K.; Rambabu, K.; Devarajulu, T.; Krishnaiah, A.; J. Chem. Eng. Data 40 (1995) 124. Senol, A.; Sayar, A. A.; Fluid Phase Equilib. 106 (1995) 169. Bhardwaj, U.; Maken, S.; Singh, K. C.; J. Chem. Eng. Data 41 (1996) 1043. Dejoz, A.; Gonzalez-Alfaro, V.; Miguel, P. J.; Vazquez, M. I.; J. Chem. Eng. Data 41 (1996) 89. Dominguez, M.; Rodriguez, S.; Lopez, M. C.; Royo, F. M.; Urieta, J. S.; J. Chem. Eng. Data 41 (1996) 37.

394 96-elb 96-gri/zhu 96-nik/jad 96-nik/mah 96-ste/chi 96-tak/uem 97-com/fra 98-ami/ban 98-ami/pat-1 98-art/dom 98-fen/cho 98-nik/shi 98-pai/che 98-pal/sha 98-sen

References El-Banna, M. M.; J. Chem. Eng. Data 42 (1996) 31. Grineva, O. V.; Zhuravlev, V. I.; Lifanova, N. V.; J. Chem. Eng. Data 41 (1996) 155. Nikam, P. S.; Jadhay, M. C.; Hasan, M.; J. Chem. Eng. Data 41 (1996) 1028. Nikam, P. S.; Mahale, T. R.; Hasan, M.; J. Chem. Eng. Data 41 (1996) 1055. Steele, W. V.; Chirico, R. D.; Knipmeyer, S. E.; Nguyen, A.; J. Chem. Eng. Data 41 (1996) 1255. Takiguchi, Y.; Uematsu, M.; J. Chem. Thermodyn. 28 (1996) 7. Comelli, F.; Francesconi, R.; J. Chem. Eng. Data 42 (1997) 705. Aminabhavi, T. M.; Banerjee, K.; J. Chem. Eng. Data 43 (1998) 509. Aminabhavi, T. M.; Patil, V. B.; J. Chem. Eng. Data 43 (1998) 504. Artigas, H.; Dominguez, M.; Mainar, A. M.; Lopez, M. C.; Royo, F. M.; J. Chem. Eng. Data 43 (1998) 580. Feng, L.-C.; Chou, C.-H.; Tang, M.; Chen, Y. P.; J. Chem. Eng. Data 43 (1998) 658. Nikam, P. S.; Shirsat, L. N.; Hasan, M.; J. Chem. Eng. Data 43 (1998) 732. Pai, Y.-H.; Chen, L.-J.; J. Chem. Eng. Data 43 (1998) 665. Pal, A.; Sharma, S.; J. Chem. Eng. Data 43 (1998) 532. Senol, A.; J. Chem. Eng. Data 43 (1998) 763

Landolt-Börnstein New Series IV/8G